m/s. greentec chemicals pvt. ltd
TRANSCRIPT
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 558
CHAPTER - 6
___________________________________________________________________________
RISK ASSESSMENT & DISASTER MANAGEMENT PLAN
In order to support the environment impact assessment and environment management
plan, following additional studies have been included in the report.
Risk assessment
Disaster Management Plan
On site and off site emergency action plan
Occupational Health and Safety Management System
6.1 RISK ASSESSMENT
6.1.1 INTRODUCTION
Hazard analysis involves the identification and quantification of the various hazards like
storage , handling & operations (unsafe conditions). On the other hand, risk assessment
deals with recognition and computation of risks, the equipment in the plant and personnel
are prone to, due to accidents resulting from the hazards present in the plant (operations)
Risk assessment follows an extensive hazard analysis. It involves the identification and
assessment of risks the neighboring populations are exposed to as a result of hazards
present. This requires a thorough knowledge of failure probability, credible accident
scenario, vulnerability of population etc. Much of this information is difficult to get or
generate. Consequently, the risk assessment is often confined to maximum credible
accident studies. It provides basis for what should be type and capacity of its on-site and off-
site emergency plan also what types of safety measures shall be required.
6.1.2 APPROACH TO THE STUDY
Risk involves the occurrence or potential occurrence of some accidents consisting of an
event or sequence of events. The risk assessment study covers the following:
Identification of potential hazard area;
Identification of representative failure cases;
Visualization of the resulting scenarios in terms of fire and explosion;
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Assess the overall damage potential of the identified hazardous events and the
impact zones form the accidental scenarios;
Furnish the recommendations on the minimization of the worst accident possibilities
Preparation of Disaster Management Plan;
Emergency Plan, which includes Occupational and Health Safety Plan;
6.1.3 METHODOLOGY
Quantitative risk assessment (QRA) is a means of making a systematic assessment of the
risks from hazardous activities, and forming a rational evaluation of their significance, in
order to provide input to a decision-making process. The term ‘quantitative risk assessment’
is widely used, but strictly this refers to the purely numerical assessment of risks without
any evaluation of their significance. The study has been conducted based on the premises of
a traditional Quantitative Risk Assessment. The key components of a QRA are explained
below, and illustrated in Figure-6.1 and Figure-6.2.
FIGURE – 6.1
QRA METHODOLOGY
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FIGURE–6.2
FLOW CHART FOR QUANTITATIVE RISK ASSESSMENT
Start Identify Risk Areas
Select a Risk Area
Identify Failure Cases
Select a Failure Cases
Identify Consequence Outcomes
Select Consequence Outcomes
Determine Frequency
Estimate Consequence
Record Frequency and Consequence in a summary Table
Have all Consequence outcomes been studied?
Have all failure cases been studied?
Have all risk areas been studied?
Draw Risk Contours Finish
Yes
Next Next
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6.1.4 HAZARD IDENTIFICATION
Identification of hazards in the proposed project activity is of primary significance of the
analysis, and quantification. Hazard states the characteristics of system/plant/process that
presents potential for an accident. All the components of a system/plant/process need to be
thoroughly examined to assess their potential for initiating or propagating an unplanned
event/sequence of events, which can be termed as an accident.
6.1.4.1 IDENTIFICATION OF HAZARDOUS AREAS
The procedure for QRA starts with identification of major risk areas in the installation.
Operation carried out in specialty and agrochemical Industries usually come under certain
board, general categories. At M/s. Greentec Chemicals Pvt. Ltd., major risk areas are as
follows:
Bulk storage area for Raw Materials (explosive, toxic, Flammable & solvent) at ambient
temperature and atmospheric pressure.
Process Plant involving pumping, transportation, reactors, distillation, heating, cooling,
etc.
Bulk loading and unloading from storage tanks to road takers and vice versa.
6.1.4.2 IDENTIFICATION OF FAILURE CASES FOR HAZARDOUS AREAS
Release due to catastrophic failure of storage tanks or process vessels.
Spillage/Overflow & Leakage from storage tank
Rupture of connected pipe with storage tank or process vessels.
Continuous release at significant rates for long durations transfer pipelines caused by
sudden, major break of the pipeline.
Continuous release at low rate through small holes or cracks in piping and vessels, flange
leaks, and leakage from pump glands and similar seals.
It is to be noted that for Quantitative Risk Assessment, worst case scenarios has been
considered, though their frequency of occurrence is much lower than the cases of small
leaks.
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6.1.4.3 MAJOR HAZARDOUS AREAS
The hazardous chemical storage area is shown in Figure-6.3. The major Hazardous chemicals
to be stored, transported, handled and utilized within the plot area are summarized in the
Table-6.1. Other hazards and control measures are summarized in Table-6.2. Facilities /
System for process safety, transportation, fire fighting system and emergency capabilities to
be adopted are stated below.
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FIGURE-6.3
HAZARDOUS CHEMICAL STORAGE AREA
-
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TABLE-6.1
STORAGE AND HANDLING DETAILS OF HAZARDOUS CHEMICALS
Quantity Name of the
Hazardous
Substance
(Mention
concentration
if any)
Maximum
that can
be stored
Actually
stored
(including
process &
handling)
Place of its
storage
State &
Operating
Pressure &
Temperature
Type of Hazard
Possible (fire,
explosion, toxic
release etc.)
Control measure provided
CHLORINE 36 MT 27 MT RM Storage
area 3
Liquefied
@ RT 10
kg/cm2
Toxic Release Online Gas Sensors, Pressure
Gauge, Emergency Kit, Caustic
Scrubbing System, SCBA Set
HYDROGEN 3000 KG 2000 KG RM Storage
area 3
Compressed
gas
Flammable Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
XYLENE 20 MT 15 MT RM Storage
area 2
Liquid Flammable Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
TOLUENE 25 KL 17 KL Solvent Yard Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
METHANOL 35 KL 25 KL Solvent Yard
RM storage
3
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
ETHANOL 30 KL 25 KL Solvent Yard
RM storage
3
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
HYDROCHLORIC
ACID
20 KL 10 KL RM Storage
1
Liquid Spillage/Leakage Bund Wall, scrubbers
CARBON
DISULPHIDE
200 KL 150 KL RM Storage
1
Liquid Fire Bund wall, Earthing – bonding,
fire fighting facility, fencing.
CAUSTIC LYE
48 %
200 KL 150 KL RM Storage
1
Liquid Spillage/Leakage Bund wall, Earthling – bonding,
fire fighting facility, fencing.
ISOPROPYL
ALCOHOL
20 KL 12 KL RM Storage
3
Liquid Fire Bund wall, Earthing – bonding,
fire fighting facility, fencing.
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Quantity Name of the
Hazardous
Substance
(Mention
concentration
if any)
Maximum
that can
be stored
Actually
stored
(including
process &
handling)
Place of its
storage
State &
Operating
Pressure &
Temperature
Type of Hazard
Possible (fire,
explosion, toxic
release etc.)
Control measure provided
PHENOL 40 KL 25 KL RM Storage
2
Liquid Fire Bund wall, Earthing – bonding,
fire fighting facility, fencing.
NITRIC ACID 20 KL 15 KL RM tank
farm 1
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
AMMONIA
SOLN. 22%
30 KL 20 KL RM tank
farm 2
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
AMMONIA GAS
CYLINDER
1000 Kg 700 Kg GTI plant
RM area
Compressed
gas
Flammable Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
ETHYLENE
DIAMINE
300 KL 250 KL RM tank
farm 1
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
PCl3 150 KL 100 KL Intermediate
plant
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
METHYLENE
DICHLORIDE
30 KL 20 KL RM Storage
2
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
ETHYLENE
DICHLORIDE
30 KL 20 KL RM Storage
2
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
ACETIC
ANHYDRIDE
50 KL 40 KL RM Storage
2
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
SULPHURIC
ACID
25 KL 20 KL RM tank
farm 1
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
DMPAT 100 KL 75 KL Intermediate
plant
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
BROMINE 15 MT 12 MT RM Storage
3
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
ETHYL ACETATE 25 KL 20 KL RM Storage
2
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
ACETONE
(DRUMS)
5 KL 4 KL RM storage
4
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
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Quantity Name of the
Hazardous
Substance
(Mention
concentration
if any)
Maximum
that can
be stored
Actually
stored
(including
process &
handling)
Place of its
storage
State &
Operating
Pressure &
Temperature
Type of Hazard
Possible (fire,
explosion, toxic
release etc.)
Control measure provided
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
HEXANE 5 KL 4 KL RM storage
4
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
MONO CHLORO
ACETIC ACID
20 KL 15 KL RM storage
3
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
TETRA HYDRO
FURAN
5 KL 4 KL RM storage
4
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
DMS
(DRUMS)
5 MT 4 MT GTI plant RM
store
Liquid Corrosive Bund wall, Earthing – bonding,
fire fighting facility, fencing.
SULPHUR
LIQUID
30 KL 20 KL Intermediate
plant
Solid Corrosive Close room, flame proof
fittings, and proper ventilation.
4 NOx
(DRUMS)
27 MT 18 MT GTH plant
RM store
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
ZINC SULPHATE
SOLU 13%
100 KL 75 KL RM tank
farm 1
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
MNSO4
SOLUTION 27%
500 KL 350 KL RM tank
farm 1
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
SODIUM
METHOXIDE
(DRUMS)
4 MT 2 MT RM store 5 Solid Fire Close room, flame proof
fittings, and proper ventilation.
ACRYLONITRILE
(DRUMS)
8 MT 6 MT RM store 5 Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
TMP
(DRUMS)
15 MT 10 MT RM store 5 Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
DIMETHYL
SULPHOXIDE
(DRUMS)
16 MT 12 MT RM store 5 Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
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Quantity Name of the
Hazardous
Substance
(Mention
concentration
if any)
Maximum
that can
be stored
Actually
stored
(including
process &
handling)
Place of its
storage
State &
Operating
Pressure &
Temperature
Type of Hazard
Possible (fire,
explosion, toxic
release etc.)
Control measure provided
METHYL ISO
BUTYL KETONE
(DRUMS)
8 MT 5 MT RM storage
6
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
BUTYL
ALCOHOL
(DRUMS)
6 MT 5 MT RM storage
6
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
PHOSPHORUS
(DRUMS)
100 MT 80 MT RM store 4 Solid at
Room Temp.
Fire Bund wall, Earthing – bonding,
fire fighting facility, fencing.
SOD CYANIDE
(DRUMS)
4 MT 3 MT RM storage
6
Solid Toxic Bund wall, Earthing – bonding,
fire fighting facility, fencing.
CO2
(CYLINDER)
8 MT 6 MT RM storage
5
Compressed
gas
Flammable Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
SO2
(CYLINDER)
4 MT 3 MT RM storage
5
Compressed
gas
Corrosive Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
THIONYL
CHLORIDE
(DRUMS)
10 MT 8 MT RM storage
6
Liquid Toxic Bund wall, Earthing – bonding,
fire fighting facility, fencing.
ORTHO
DICHLORO
BENZENE
(DRUMS)
6 MT 5 MT RM storage
6
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
DIMETHYL
FORMAMIDE
(DRUMS)
10 MT 8 MT RM storage
6
Liquid Fire Control Measures has been
taken as per license approved
by Dept. of Explosives.
Flameproof area, static
Earthing, fire fighting facility,
flame arrester, fenced area.
DI METHYL
AMINE
(DRUMS)
8 MT 6 MT RM storage
6
Liquid Fire & Toxic Bund wall, Earthing – bonding,
fire fighting facility, fencing.
MONO METHYL
ACETO
ACTEMIDE
(DRUMS)
10 MT 6 MT RM storage
6
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
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Quantity Name of the
Hazardous
Substance
(Mention
concentration
if any)
Maximum
that can
be stored
Actually
stored
(including
process &
handling)
Place of its
storage
State &
Operating
Pressure &
Temperature
Type of Hazard
Possible (fire,
explosion, toxic
release etc.)
Control measure provided
ANILINE
(DRUMS)
12 MT 8 MT RM storage
6
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
FORMIC ACID 20 MT 15 MT RM storage
2
Liquid Spillage/leakage Bund wall, Earthing – bonding,
fire fighting facility, fencing.
SODIUM LIGNO
SULPHATE
(BAGS)
30
25 RM storage
6
Solid leakage No hazard
HMTA
(BAGS)
20 15 RM storage
6
Solid leakage No hazard
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TABLE 6.2
OTHER HAZARDS AND CONTROL
Sr.
No.
Name of the possible
hazard or emergency Its sources & reasons
Its effects on persons,
property & environment In charge person
Place of
its effect Control measures provided
Name and
designation
1 2 3 4 5 6 7
1 BOILER
(1) Burning
(2) Physical injury
(3) Explosion
Over pressure in the boiler if
safety valve not working. Water
level indicator not working.
Low water level indicator fail.
High temp. System fails.
Minor/Major Injury Loss
of human life Loss of
property (Loss of Man /
Machine Material)
Utility Block Lower & Upper Level Indication System provision. Safety valves for
pressure control fixed temp. & pressure indicator provided. Blow down
& blowing system provided for cleaning tube and shell. Soft water
used. Inter locking provided on pumps, FD fan, ID fan. Periodical
checking & inspection maintenance done. Yearly inspection done by
Boiler Inspector
Engineering Services
2 ELECTRICITY
(1) Burning
(2). Fire
(3). Shock
Loose Contacts, Weak earthing
Short Circuit Improper
Insulation
Burning, Shock, Death Surrounding
the accident
area
Proper Earthing, Periodical Checking of joints, proper insulations of
Equipments, etc. Flame proof fitting in solvent storage area, bounding
and jumpers to all solvent barrier lines provided.
Electrical engineer
3 HOUSE KEEPING
(1). Physical
(2). Burning
(3) Fire
(4) Chemical Exposure
Bad House keeping Physical / Chemical
Thermal Burn Injury
(Major / Minor)
All Plant Proper Handling, regular cleaning, Proper placement of material (RIGHT
THING AT THE RIGHT PLACE)
Personnel depat
4 PIPE LINE LEAKAGES
Spillages etc.
(1) Corrosion
(2) Toxic gas release
Leaking of pipe line due to
corrosion, Loose contact etc.
Physical / Chemical
Thermal Burn Injury
(Major /
Minor)/Chemical
Exposure
Plant area Proper maintenance, Proper Selection of Material for pipe lines,
Immediate attention, NO SMOKING Boards displayed.
Concerned Plant In
Charge
5 Natural Gas Leaking of pipe line due to
corrosion
Leakage from flange joint
Loose earthing / Loose contact
etc.
Fire & explosion Plant area Proper maintenance, Proper Selection of Material for pipe lines,
Numetic test as per regulations
NO SMOKING Boards displayed.
Concerned Plant In
Charge
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TABLE 6.3
HAZARDOUS PROPERTIES OF THE CHEMICALS, COMPATIBILITIES, SPECIAL HAZARD AND ANTIDOTES
SR. NAME OF
CHEMICAL
HAZARD FLASH
POINT 0
C
BP 0
C
LEL % UEL % SP.GR.
20 0
C
VD SOLUBILITY
WITH WATER
at 20 0 C
NFPA
H F R
HAZARDOUS
COMBUSTION
PRODUCT
TLV
/
TWA
IDLH
LC50
LD50
1. CHLORINE
CAS # 7782-50-5
T - -34.6 - - - 2.5 Reacts 4 0 0 When Heated, It Emits
Highly Toxic Fumes
0.5 ppm 10 ppm 293 ppm (Rat)
1 Hr
-
2. HYDROGEN
CAS# 1333-74-0
F - -253.15 4 74.5 - 0.07 Insoluble 0 4 2 - - - -
-
3. XYLENE
CAS#1330-20-7
F 24 138.5 1 7 0.864 3.7 Insoluble in
cold water, hot
water
2 3 0 Carbon Oxides (CO,
CO2)
- - 2119 5000 mg/kg
(Rat)
4. TOLUENE
CAS # 108-88-3
F 4 110.6 1.2 8 0.863 3.2 700 mg/L 2 3 0 Moderately Dangerous;
When Heated, Emits
Toxic Fumes Which Can
React Vigorously With
Oxidizing Materials
50 ppm 500 ppm 49 gm/m3
(Rat) 4Hr
636 mg/kg
(Rat)
5. METHANOL
CAS#67-56-1
F 12 64.5 6 36.5 0.7915 1.11 Easily soluble
in cold water,
hot water
2 3 0 Carbon Oxides (CO,
CO2)
200 - 5628 64000
mg/kg
(Rat)
6. ETHANOL
CAS# 64-17-5
F 12.78 78.5 /
-114.1
3.3 19 0.789 1.59 Easily soluble
in cold water,
hot water
2 3 0 Carbon Oxides (CO,
CO2)
1000 - 7060 20000
mg/kg
(Rat)
7. HYDROCHLORIC
ACID
CAS # 7647-01-0
C 11 -85.06 - - 1.19 1.25 Soluble 3 0 1 Non-Combustible,
Substance Itself Does
Not Burn But May
Decompose Upon
Heating To Produce
Corrosive And/Or Toxic
Fumes
5 ppm 50 ppm 4701 ppm
0.5 Hr [Rat]
-
8. CARBON
DISULPHIDE
CAS#75-15-0
F -30 46.3 1.3 50 1.2632 2.63 Very slightly
soluble in cold
water
3 3 0 - 10 ppm 500 2780 12500
mg/kg
(Rat)
9. CAUSTIC LYE 48 %
CAS#1310-73-2
C - 1388 - - 2.13 - Easily soluble
in cold water
3 0 2 Non - Flammable 2 (mg/m3) 250
mg/m3
500 -
10. ISOPROPYL
ALCOHOL
CAS # 67-63-0
F 12 82.4 2 12.7 0.785 2.1 Soluble 1 3 0 Fire May Produce
Irritating, Corrosive
And/Or Toxic Gases
400 ppm 2000
ppm
100000 mg/l
96 Hr
5045 gm/kg
[Rat]
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SR. NAME OF
CHEMICAL
HAZARD FLASH
POINT 0
C
BP 0
C
LEL % UEL % SP.GR.
20 0
C
VD SOLUBILITY
WITH WATER
at 20 0 C
NFPA
H F R
HAZARDOUS
COMBUSTION
PRODUCT
TLV
/
TWA
IDLH
LC50
LD50
11 PHENOL
CAS#108-95-2
F 79 182 1.7 8.6 1.057 3.24 Soluble in cold
water,
Solubility in
water: 1g/15
ml water
3 2 0 Carbon Oxides (CO,
CO2)
5 ppm 250 ppm 317 -
12
NITRIC ACID
CAS #7697-37-2
C - 121 - - 1.408 2.5 Easily soluble
in cold water,
hot water
3 0 0 Non Flammable 2 ppm 25 ppm - 244 ppm 0.5
hours [Rat]
13 AMMONIA SOLU22
%
CAS#1336-21-6
T & C - 38 - - 0.898 - Easily soluble
in cold water
3 0 0 Non Flammable 25 ppm - - 2000 ppm 4
hours [Rat]
14 AMMONIA GAS
CAS#7664-41-7
T & C - -33.4 - - - - Easily soluble
in cold water
3 0 0 Non Flammable 25 ppm 500 ppm - 2000 ppm 4
hours [Rat]
15 PCL3
CAS#7719-12-2
T & C - 76 - - 1.574 4.75 Insoluble in
water
3 0 2 Non Flammable 0.5 ppm 25 ppm 18 mg/kg [Rat] 50 ppm 4
hours
[Guinea pig]
16 METHYLEN
DICHLORIDE
CAS#75-09-2
T - 39.75 12 19 1.3266 2.93 Partially
soluble in cold
water
2 1 0 Carbon Oxides (CO,
CO2), Halogenated
Compounds
50 - 1,600 52000
mg/kg
(Rat)
17 ETHYLEN
DICHLORIDE
CAS#107-06-2
F 13 83.5 6.2 15.6 1.2351 3.42 Very slightly
soluble in cold
water
2 3 0 Carbon Oxides (CO,
CO2)
75 - 670 1414.2
mg/kg
(Rat)
18 ACETIC ANHYDRIDE
CAS#: 108-24-7
F T C 49 139.9 2.7 10.3 1.08 3.52 - 3 2 0 Carbon Oxides (CO,
CO2)
5 ppm 1,000
ppm
1780 mg/kg
[Rat]
-
19 DMPAT
CAS#17321-47-0
- - - - - - - - Carbon Monoxide,
Nitrogen Oxides, Sulfur
Oxides
- - - -
20 BROMINE
CAS#: 7726-95-6
T & C - 58.78 - - 3.11 7.1 Very slightly
soluble in cold
water
3 0 0 Non Flammable 0.1 ppm 10 ppm 2,600 ppm 240 ppm
21 ETHYL ACETATE
CAS#141-78-6
F -4.4 77 2.2 9 0.902 3.04 Soluble in cold
water, hot
water
2 3 0 Carbon Oxides (CO,
CO2)
400 ppm 10,000
ppm
5620 mg/kg
[Rat]
45000 mg/m
3 hours
[Mouse]
22 ACETONE
CAS#67-64-1
F -20 56.2 2.6 12.8 0.79 2 Easily soluble
in cold water,
hot water
2 3 0 Carbon Oxides (CO,
CO2)
500 - 5,800 44000
mg/kg
(Rat)
23 HEXANE F -22.5 68 1.15 7.5 0.66 2.97 Insoluble in 2 3 0 Carbon Oxides (CO, 500 - 25000 -
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 572
SR. NAME OF
CHEMICAL
HAZARD FLASH
POINT 0
C
BP 0
C
LEL % UEL % SP.GR.
20 0
C
VD SOLUBILITY
WITH WATER
at 20 0 C
NFPA
H F R
HAZARDOUS
COMBUSTION
PRODUCT
TLV
/
TWA
IDLH
LC50
LD50
CAS#110-54-3 cold water,
hot water
CO2)
24 MONO CHLORO
ACETIC ACID
CAS#: 79-11-8
T & C 150 189 8 - 1.4043 - Soluble in cold
water, hot
water
3 1 0 Carbon Oxides (CO,
CO2), Halogenated
Compounds
0.05 ppm - 55 mg/kg
[Rat]
254.6 ppm 4
hour(s) [Rat]
25 TETRA HYDRO
FURAN
CAS#109-99-9
F & T -14.5 65 2 11.8 0.8892 2.5 Partially
soluble in cold
water.
Solubility in
water is 30%.
2 3 0 Carbon Oxides (CO,
CO2)
200 ppm 2000
ppm
1650 mg/kg
[Rat]
21000 mg/m
3 hours [Rat]
26 DMS
CAS#77-78-1
T & C 83.3 - - - 1.3322 4.35 Partially
soluble in cold
water
4 2 0 Carbon Oxides (CO,
CO2), Sulfur Oxides
(SO2, SO3)
1 ppm 10 ppm 205 mg/kg
[Rat]
45 ppm 4
hour(s) [Rat]
27 SULPHER
CAS#7704-34-9
C 207 445 - - Density:
2.07
- Insoluble in
cold water, hot
water
2 2 0 Sulfur Oxides (SO2, SO3) 5 ppm 100 ppm >8437 mg/kg
[Rat]
--
28 4 NOX
CAS#99-51-4
113 143 - - 1.139 - - - Carbon Oxides,
Nitrogen Oxides (NOx)
- - - -
29 ZNSO4 SOL 13%
CAS#7446-20-0
- - - - - - Soluble in
water. Water:
170 g/100ml
2 0 0 On Burning: Release Of
Toxic And Corrosive
Gases/Vapors (Sulphur
Oxides, Zinc Oxide) And
Formation Of Metallic
Fumes
- - - -
30 MNSO4 SOL 27 %
CAS#10034-96-5
- - 850 - - 2.95 - Easily soluble
in cold water,
hot water
2 0 0 - - 500
mg/m3
(as Mn)
- -
31 SOD METHOXIDE
CAS#124-41-4
F 33 - 7.3 36 1.1 1.1 Soluble in cold
water.
Decomposes/r
eacts in water
2 2 2 Carbon Oxides (CO,
CO2)
10 mg/m3 -- 2037 mg/kg
[Rat]
--
32 ACRYLONITRILE
CAS#: 107-13-1
F & T -1.111 77.3 3.1 17 0.806 1.8 Very slightly
soluble in cold
water, hot
water
3 3 1 Carbon Oxides (CO,
CO2)
1 ppm 85 ppm 78 mg/kg [Rat] 333 ppm 4
hours [Rat]
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 573
SR. NAME OF
CHEMICAL
HAZARD FLASH
POINT 0
C
BP 0
C
LEL % UEL % SP.GR.
20 0
C
VD SOLUBILITY
WITH WATER
at 20 0 C
NFPA
H F R
HAZARDOUS
COMBUSTION
PRODUCT
TLV
/
TWA
IDLH
LC50
LD50
33 TMP
CAS#512-56-1
T > 150 197 - - 1.210 -
1.215
g/cm3
- 1,000 g/l at 25
°C
Combustible. Fire may
cause evolution of:
oxides of phosphorus
- - - -
34 DIMETHYL
SULHOXIDE
CAS#67-68-5
T & F 89 189 2.6 42 1.1008 2.71 Soluble in cold
water, hot
water
1 2 0 Carbon Oxides (CO,
CO2), Sulfur Oxides
(SO2, SO3)
- - 14500 -
35 BUTYL ALCHOL
CAS#: 71-36-3
F & T 28.9 117.7 1.4 11.2 0.81 2.55 Partially
soluble in cold
water, hot
water
1 3 0 Carbon Oxides (CO,
CO2)
100 ppm 8,000
ppm
790 mg/kg
[Rat.]
3400 mg/kg
[Rabbit.]
36 SOD CYNIDE
CAS#: 143-33-9
T - 1496 - - 1.595 HCN
gas:
0.941
Soluble in cold
water
3 1 0 Some Metallic Oxides 5 mg/m3 25
mg/m3
6.44 mg/kg
[Rat]
10.4 mg/kg
[Rabbit]
37 SO2
CAS#7446-09-5
T & C - - - - - 1.5 Soluble in cold
water
3 0 0 - 2 ppm 100 ppm - 1260
ppm/4h
38 CO2
CAS#124-38-9
T - -78.5 - - - 1.53 Soluble in cold
water
1 0 3 Carbon Oxides (CO,
CO2)
5000 ppm 40,000
ppm
- -
39 THIONYL CHLORIDE
CAS#: 7719-09-7
T - 76 - - 1.638 4.1 Insoluble in
cold water
3 0 2 - 1 ppm - - 500 ppm 1
hours [Rat]
40 ORTHOFICHLORO
BENZENE
CAS#: 95-50-1
F 66 2.2 9.2 1.3059 5.07 Very slightly
soluble in cold
water
2 2 0 Carbon Oxides (CO,
CO2), Halogenated
Compounds
50 ppm 200 ppm - 500 mg/kg
[Rat]
41 DI METHYL
FORMAMIDE
CAS#68-12-2
F & T 57.77
8
153 2.2 15.2 0.949 2.51 Easily soluble
in cold water,
hot water
2 2 0 Carbon Oxides (CO,
CO2), Nitrogen Oxides
(NO, NO2)
10 - 4720 9400 mg/kg
(Rat)
42 DIMETHYL AMINE
CAS#124-40-3
F -6.69 7 2.8 14.4 0.84 0.62 Easily soluble
in cold water
3 1 0 Carbon Oxides (CO,
CO2)
- - 698 4540 mg/kg
(Rat)
43 TETRA HYDRO
FURAN
CAS#109-99-9
-14.5 65 2 11.8 0.8892 2.5 Partially
soluble in cold
water.
Solubility in
water is 30%
2 3 0 Carbon Oxides (CO,
CO2)
200 ppm 2000
ppm
1650 mg/kg
[Rat]
21000 mg/m
3 hours [Rat]
44 MONO CHLORO
ACETIC ACID
CAS#: 79-11-8
T & C 150 189 8 - 1.4043 - Soluble in cold
water, hot
water
3 1 0 Carbon Oxides (CO,
CO2), Halogenated
Compounds
0.05 ppm - 55 mg/kg
[Rat]
254.6 ppm 4
hour(s) [Rat]
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 574
SR. NAME OF
CHEMICAL
HAZARD FLASH
POINT 0
C
BP 0
C
LEL % UEL % SP.GR.
20 0
C
VD SOLUBILITY
WITH WATER
at 20 0 C
NFPA
H F R
HAZARDOUS
COMBUSTION
PRODUCT
TLV
/
TWA
IDLH
LC50
LD50
45
MONOMETHLL
ACETO ACETMIDE
CAS#5977-14-0
- - 139
140
- - Bulk
density 0.8
g/l at 20 °C
- - - Carbon Oxides,
Nitrogen Oxides (NOx)
- - - > 5,000
mg/kg
46 ANILINE
CAS#: 62-53-3
T & C 70 184.1 1.3 23 1.0216 3.22 Soluble in cold
water, hot
water
2 2 0 Carbon Oxides (CO,
CO2), Nitrogen Oxides
(NO, NO2)
5 ppm 100 ppm - 250 mg/kg
[Rat.]
47 FORMIC ACID
CAS# 64-18-6
F & T 69 100 18 57 1.21 1.59 Soluble in cold
water, hot
water
3 2 0 Carbon Oxides (CO,
CO2)
5 ppm 30 ppm 6200 mg/m
0.25 hours
[Mouse]
700 mg/kg
[Mouse]
48 SOD
LIGHNOSULPHATE
CAS#: 8061-51-6
- - - - - - Easily soluble
in cold water,
hot water
2 1 0 - - - - 6030 mg/kg
[Mouse]
49 HMTA
CAS#100-97-0
F 250 - - - 1.331 4.9 Soluble in cold
water
2 1 0 Carbon Oxides (CO,
CO2), Nitrogen Oxides
(NO, NO2)
- - - 569 mg/kg
[Mouse]
50 NITRO BENZENE
CAS#: 98-95-3
T 87.78 210.8 1.8 - 1.2 4.25 Very slightly
soluble in cold
water
3 2 0 Carbon Oxides (CO,
CO2), Nitrogen Oxides
(NO, NO2)
1 ppm 200 ppm - 590 mg/kg
[Mouse]
51 ANILINE
CAS#: 62-53-3
T & C 70 184.1 1.3 23 1.0216 3.22 Soluble in cold
water, hot
water
2 2 0 Carbon Oxides (CO,
CO2), Nitrogen Oxides
(NO, NO2)
5 ppm 100 ppm - 250 mg/kg
[Rat.]
52 HYDROQUINONE
CAS#: 123-31-9
T & C 165 286 - - 1.33 3.81 Soluble in cold
water, hot
water
2 1 0 Carbon Oxides (CO,
CO2)
2 mg/m3 50
mg/m3
- 320 mg/kg
[Rat.]
53 METHYL BROMIDE
CAS#: 74-95-3
T - 96.95 - - 2.497 6.05 Insoluble in
cold water, hot
water
2 0 0 - 20 ppm 250 ppm 3977.9 ppm 4
hour(s) [Rat]
108 mg/kg
[Rat]
54 ETHYL BROMIDE
CAS#: 74-96-4
F & T -10 38.04 6.75 11.25 1.45 3.76 Very slightly
soluble in cold
water, hot
water
2 3 2 Carbon Oxides (CO,
CO2)
200 ppm 2000
ppm
8115 ppm 4
hour(s)
[Mouse]
1350 mg/kg
[Rat]
55 DETCL
CAS#2524-04-1
C 113 45 - - - - - - Carbon Oxides, Sulphur
Oxides, Oxides Of
Phosphorus, Hydrogen
Chloride Gas
- - - 1,340
mg/kg
(Rat)
56 HYDROGEN C - 108 - - 1.1 1.1 Easily soluble 3 0 1 - 1 ppm 75 ppm 2000 mg/m 4 2000 mg/kg
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 575
SR. NAME OF
CHEMICAL
HAZARD FLASH
POINT 0
C
BP 0
C
LEL % UEL % SP.GR.
20 0
C
VD SOLUBILITY
WITH WATER
at 20 0 C
NFPA
H F R
HAZARDOUS
COMBUSTION
PRODUCT
TLV
/
TWA
IDLH
LC50
LD50
PEROXIDE
CAS#7722-84-1
in cold water hours [Rat] [Mouse]
57 CHLORAL
CAS#: 302-17-0
75 96 - - 1.9081 - Easily soluble
in cold water
2 1 0 Carbon Oxides (CO,
CO2), Halogenated
Compounds
- - - 479 mg/kg
[Rat]
58 ETHYL BROMIDE
CAS#: 74-96-4
F & T -10 38.04 6.75 11.25 1.45 3.76 Very slightly
soluble in cold
water, hot
water
2 3 2 Carbon Oxides (CO,
CO2)
200 ppm 2000
ppm
8115 ppm 4
hour(s)
[Mouse]
1350 mg/kg
[Rat]
59 METHYL BROMIDE
CAS#: 74-95-3
T - 96.95 - - 2.497 6.05 Insoluble in
cold water, hot
water
2 0 0 - 20 ppm 250 ppm 3977.9 ppm 4
hour(s) [Rat]
108 mg/kg
[Rat]
60 MONO CHLORO
ACETIC ACID
CAS#: 79-11-8
T & C 150 189 8 - 1.4043 - Soluble in cold
water, hot
water
3 1 0 Carbon Oxides (CO,
CO2), Halogenated
Compounds
0.05 ppm - 55 mg/kg
[Rat]
254.6 ppm 4
hour(s) [Rat]
61 HYDRAZINE HYDRIDE
(80%)
CAS#: 7803-57-8
C & T 72 113.5 4.7 - 1 1.1 Easily soluble
in cold water,
hot water
3 2 2 - - - 570 ppm 4
hour(s) [Rat]
129 mg/kg
[Rat]
62 OLEUM
CAS#: 8014-95-7
C - 45 - - 1.92 3.4 Easily soluble
in cold water
3 0 2 - 2 ppm - 510 mg/m 2
hours [Rat]
2140 mg/kg
[Rat.]
63 PHENYL HYDRAZINE
CAS#: 100-63-0
T 89 238 - - 1.099 3.7 Easily soluble
in cold water
3 2 0 Carbon Oxides (CO,
CO2), Nitrogen Oxides
(NO, NO2)
5 ppm 15 ppm - 188 mg/kg
[Rat]
64 M CRESOL
CAS#: 108-39-4
F 86 202 1.1 - 1.034 3.72 Partially
soluble in cold
water Soluble
in about 40
parts water
3 2 0 Carbon Oxides (CO,
CO2)
5 ppm 250 ppm 1100 mg/kg
[Rat]
242 mg/kg
[Rat]
65 NITROSYL
SULPHONIC ACID
(40%)
CAS#7782-78-7
F & C - > 100 - - - - Decomposes - Carbon Oxides (CO,
CO2), Nitrogen Oxides
(NO, NO2)
- - 320 mg/m3 2140 mg/Kg
66 CYNO ACETIC ACID
CAS#: 3722-09-8
C 160 108 - - - - - 3 1 0 Carbon Oxides (CO,
CO2), Nitrogen Oxides
- - - 1500 mg/kg
[Rat]
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 576
SR. NAME OF
CHEMICAL
HAZARD FLASH
POINT 0
C
BP 0
C
LEL % UEL % SP.GR.
20 0
C
VD SOLUBILITY
WITH WATER
at 20 0 C
NFPA
H F R
HAZARDOUS
COMBUSTION
PRODUCT
TLV
/
TWA
IDLH
LC50
LD50
(NO, NO2)
67 NPMIDA
CAS#5994-61-6
C - - - - - - - - Carbon Oxides,
Nitrogen Oxides (NOx),
Oxides Of Phosphorus
- - - -
68 BENZYL CHLORIDE
CAS#: 100-44-7
F & C 67.2 179 1.1 14 1.1 4.36 Insoluble in
cold water, hot
water
3 2 0 Carbon Oxides (CO,
CO2), Halogenated
Compounds
1 ppm 10 ppm - 1231 mg/kg
[Rat.]
69 TCAC
CAS#: 76-03-9
C - 195.5 - - 1.6126 - Easily soluble
in cold water,
hot water,
Solubility in
water @ 25
deg. C: 1000
g/100 ml water
3 0 0 - 1 ppm - - -
F = FIRE T = TOXIC
E = Explosive R = REACTIVE
BP = BOILING POINT LEL = LOWER EXPLOSIVE LIMIT
UEL = UPPER EXPLOSIVE LIMIT SP.GR = SPECIFIC GRAVITY
VD = VAPOUR DENSITY ER = EVAPORATION RATE
H = HEALTH HAZARD CLASS F = FIRE HAZARD CLASS
R = REACTIVE HAZARD BR = BURNING RATE
TLV = THRESHOLD LIMIT VALUE PPM = PARTS PER MILLION
STEL = SHORT TERM EXPOSURE LIMIT NFPA = NATIONAL FIRE PROTECTION ASSOCIATION-USA
C = C
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 577
6.1.4.4 CONTROL MEASURES WHILE STORAGE OF HAZARDOUS CHEMICALS
For PESO Underground Storage Tank Farm:
Class A petroleum products will be received through road tanker and stored in
underground storage tank as per petroleum rules.
Tank farm will be constructed as per explosive department requirement and separation
distance will be maintained.
Static earthing provision will be made for road tanker as well as storage tank.
Flame arrestor with breather valve will be provided on vent line.
Road tanker unloading procedure will be prepared and implemented.
Fire load calculation will be done and as per fire load Hydrant System will be provided as
per NFPA std. and Fire extinguishers will be provided as per fire load calculation.
Spark arrestor will be provided to all vehicles in side premises.
Flame proof type equipment s and lighting will be provided.
Lightening arrestor will be provided on the top of chimney.
Trained and experience operator will be employed for tank farm area.
NFPA label (hazard identification) capacity and content will be displayed on storage tank.
Solvents will be transferred by pump only in plant area and day tank will be provided.
Overflow line will be return to the storage tank or Pump On-Off switch will be provided
near day tank in plant.
Jumpers will be provided on solvent handling pipe line flanges.
Flexible SS hose will be used for road tanker unloading purpose and other temp.
Connection.
For Above Ground Non PESO Storage Tank Farm:
SS storage tank provided as per IS code.
Dyke wall provided to storage tank.
Level gauge provided with low level high level auto cut-off provision.
Fire hydrant monitor with foam trolley facility provided.
FLP type pump provided.
Double static earthing provided to storage tank.
Double Jumper clip provided to all pipeline flanges.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 578
Road tanker unloading procedure prepared and implemented.
Lightening arrestor, PPEs provided.
Safety shower, eye wash provided.
NFPA labeling system adopted for drums as well as storage tanks.
Safety Measures for Acid Storage Tank Area:
Storage tank will be stored away from the process plant.
Tanker unloading procedure will be prepared and implemented.
Caution note and emergency handling procedure will be displayed at unloading area and
trained all operators.
NFPA label will be provided.
Required PPEs like full body protection PVC apron, Hand gloves, gumboot, Respiratory
mask etc. will be provided to operator.
Neutralizing agent will be kept ready for tackle any emergency spillage.
Safety shower, eye wash with quenching unit will be provided in acid storage area.
Material will be handled in close condition in pipe line.
Dyke wall will be provided to all storage tanks, collection pit with valve provision.
Double drain valve will provided.
Level gauge will be provided on all storage tanks.
Safety permit for loading unloading of hazardous material will be prepared and
implemented.
TREM CARD will be provided to all transporters and will be trained for transportation
Emergency of Hazardous chemicals.
Fire hydrant system with jockey pump as per TAC norms will be installed.
Bromine Storage & Handling Safety
The amount of bromine in storage will be kept to a minimum.
Minimize the dispersal of bromine vapors by locating the storage area on low ground.
Low curbs or walls (called dikes), 200 mm high, will be provided to protect the area from
external flooding and to minimize the dispersal of bromine vapors. The minimum dyked
volume will be equivalent to the largest storage tank plus 10%.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 579
Adequate size sump will be provided for collecting bromine spills and pump away
collected rainwater and fire-fighting water.
Floors will be of impervious construction, preferably concrete.
Bromine ISO tank should be stored no closer than 10 meters from human or animal
consumable articles. Explosives and flammable materials should not be stored close to
bromine.
There should be a strengthened approach way for emergency vehicles on two sides of
the installation.
Hoses will be PTFE with stainless steel braid covering and carbon steel flanges. Screwed
fittings will not used.
Provide lightning protection.
There would be sufficient bromine storage tank capacity or an empty ISO tank to
accommodate the transfer of bromine from a leaking container
Area where bromine will be used or stored will be enclosed so that unauthorized persons
and animals are prevented from entering the area. Adequate lighting will be provided to
allow sufficient night surveillance. Surveillance will be provided 24 hours a day.
Personnel escape routes will be clearly marked and it will be maintained without any
obstructions including adequately sized doors and windows.
Facilities like offices, eating, showering and changing rooms, will be located in up wind
direction and remote from the area where bromine is handled or stored. Provide an
adequate supply of clean water for washing and showers.
Emergency siren, telephone will be provided in storage area for the reporting of
accidents or emergency situations. The emergency telephone numbers will be displayed
at prominent locations and it include the fire department, ambulance service, emergency
response team, hospital and police.
A wind sock will be provided which will clearly visible from all points on the site and
replaced as required. This is required for indicating wind strength and direction.
Emergency respirator equipment cabinets (Cupboard) will be installed not more than 30
meters or ten seconds walking distance from any location in the storage area.
Showers and eyewash fountains will be provided, clearly marked, well lit and with
unobstructed access.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 580
Signs will be posted prominently at the site entrance and throughout the installation with
area maps showing access ways, hydrant locations, emergency showers, location of
emergency equipment and emergency telephone numbers.
All management and operating personnel involved in the use or handling of bromine will
undergo safety training, in addition to specific task training.
Only experienced well-trained operators will be allowed to receive and unload bromine
receptacles.
The management will ensure that emergency response plans have been made and
coordinated with the emergency response local authorities.
Bromine glass bottle capacity 2.5 litters and six bottles are stored in one packing box.
Bromine will be stored in dry and cool place and well ventilated area.
Safety permit for hazardous material loading unloading will be prepared and
implemented.
Fire hydrant system and water sprinkler system installed at tank farm area.
Safe Transportation Procedure to be adopted for Bromine ISO container
The driver and assistant driver of any vehicle transporting bromine should comply with the
following requirements:
GPS will be installed in all the trucks and ISO container vehicle.
Driver and assistant will be trained in using GPS.
Open space separated from public highway and public dwellings, where public does not
normally pass. No passengers are allowed.
The crew shall know how to use fire-fighting appliances.
The driver or driver's assistant may not open a package containing bromine.
Bromine receptacles are not to be checked with open flames.
No smoking is permitted around the transport unit or in the vicinity of the vehicle during
handling operations.
The engine is to be shut off during all handling operations unless required to drive
pumps, hoist, etc.
Parking brakes are to be applied whenever parked.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 581
If the vehicle is parked on a road at night or with poor visibility, warning signs are to be
placed 10 meters ahead of and behind the vehicle.
TREM CARD provided to all transporters and trained for transportation Emergency of
Hazardous chemicals.
Following Personal Protective Equipments are to be made compulsory when handling
Bromine
American National Standards Institute (ANSI) approved chemical safety goggles at all
times when handling Br2.
Use a full face shield over eyewear.
Full body protection PVC suite
Eyewash fountains should be located in areas where bromine is handled, used or stored.
When in danger of contact with liquid bromine, wear an approved chemical resistant
suit.
Leather or other non-woven ANSI approved steel-toed shoes or Gum boot
Protective rubber boots should be worn over shoes for extra protection.
Have NIOSH approved respirators and self-contained breathing apparatus available.
Gloves: 100% Nitrile rubber gloves or Neoprene gloves
Safety Practices in the Work Area
We will inform our all employees of the potential hazards of contact with bromine and
train them in appropriate first-aid procedures.
Bromine handling areas will be clearly marked and restricted to qualified, trained
personnel only.
Ventilation
We will maintain bromine vapor concentration in the work area to less than 0.1 ppm
with adequate exhaust hoods, ventilation systems and scrubbers. Analyze air for proper
control.
Transfer or repackage bromine only in a controlled, closed environment.
Exhaust ventilating systems will be used in enclosed areas where bromine is handled.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 582
Neutralization in Case of Spillage Leakage
Neutralization with sodium Bisulfite requires 3 moles of sodium hydroxide: 1 mole
sodium Bisulfite: 1 mole bromine.
Neutralization with sodium sulfite requires 2 moles sodium hydroxide: 1 mole sodium
sulfite: 1 mole bromine.
The weights and volumes specified include a 10% excess of sodium hydroxide and
sodium bisulfate or sodium sulfite.
Emergency Procedures
In case of bromine emergencies, follow recommended first aid and emergency response
procedures adopted
Transportation Emergencies
In emergency situations resulting from vehicle accidents:
Notify the local police, fire departments, emergency responders and the carrier.
Isolate the area.
Any person not dressed in proper protective clothing and not using a NIOSH approved
self-contained breathing apparatus should be kept a safe distance away.
Call to the supplier
Seek immediate medical assistance for those injured and follow recommended first aid
procedures.
Leaking Containers
When handling a leaking bottle personal protective clothing, goggles and NIOSH
approved self contained breathing equipment must be worn.
Clear contaminated area of non-essential personnel and send them to assembly point.
Maintain a slight ammonia atmosphere throughout the clean up. Carefully release
anhydrous ammonia gas to neutralize bromine vapor. The ammonia gas will convert
bromine to white ammonium bromide “Smoke.”
Do not allow liquid bromine and liquid ammonia to combine; a violent reaction will
occur. Ammonia (16 to 25% by volume) can form an explosive mixture with air. Pour
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 583
hypo solution*, lime and water slurry or soda ash solution over the spill. Hypo-bromine
reactions produce hydrobromic acid.
Dry sodium thiosulphate and liquid bromine produce a violent reaction; do not mix them.
Using cold water, wash neutralized bromine into a sump for transfer to an approved
waste disposal facility where the waste can be processed.
Ventilate the area to remove the ammonium bromide and any bromine fumes. Scrub the
floors and equipment with soap and water.
First Aid Procedure
Immediate medical assistance is required if bromine is swallowed, inhaled or has
contacted the eyes or skin.
If bromine has been ingested, do not give anything by mouth. Seek medical attention
immediately. Do not induce vomiting.
If bromine has been inhaled, move the exposed person to a well ventilated area. Seek
medical attention immediately. The victim should be placed in a comfortable sitting or
partly reclining position. The exposed individual should avoid exertion. If vomiting occurs,
turn the patient on his side to avoid choking. Keep the patient warm. If the patient is
coughing and showing signs of respiratory distress, properly trained personnel should
administer oxygen.
For skin contact, the affected area must be flooded immediately with large amounts of
clean water from a safety shower or other appropriate source of flowing water. Seek
medical attention immediately. All contaminated clothing, including shoes, should be
removed as quickly as possible while the victim is under the shower. Washing should be
continued for a minimum of 30 minutes. If possible, continue to wash the affected area
during transport to medical facilities. (Extended wash times of two hours or more have
proven beneficial.)
If bromine liquid or vapor contacts the eyes, they must be irrigated immediately with
large amounts of running water. Eye wash stations are preferable for irrigation. If one is
not available, a hose, water source with a liberal, gentle flow may be utilized. The eyelids
must be held apart during irrigation to ensure contact of water with all accessible tissues
of the eyes and lids. Eyes should be washed continuously for a minimum of 30 minutes. If
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 584
possible, continue flushing the eyes while transporting the employee to a physician. In all
cases of bromine injury, obtain immediate medical attention. Provide emergency
personnel with information about all materials used by the person and provide
appropriate information about bromine and first aid procedures.
For Drum Storage Area:
Some chemicals will be received at plant in drums by road truck and stored in a separate
drum storage area.
FLP type light fittings will be provided.
Proper ventilation will be provided in Godown.
Proper label and identification board /stickers will be provided in the storage area.
Conductive drum pallets will be provided.
Drum handling trolley / stackers/fork lift will be used for drum handling.
Separate dispensing room with local exhaust and static earthing provision will be made.
Materials will be stored as per its compatibility study and separate area will be made for
flammable, corrosive and toxic chemical drums storage.
Smoking and other spark, flame generating item will be banned from the Gate.
For Chlorine:
Following steps will be adopted:
SOP will be prepared for safe handling of Chlorine tonners.
Chlorine Emergency Kit will be procured and kept ready at chlorine shed.
Chlorine Hood with blower will be provided with scrubbing arrangement.
Safety Shower and eye wash will be provided in Chlorine shed area.
Tonner handling EOT crane will be installed in Chlorine shed area for safe Tonner
handling.
Safety Valve will be provided on chlorine header line and it will be connected to caustic
scrubber.
SCBA sets will be kept ready at chlorine handling area.
Safety valve will be provided on vaporizer header and outlet of safety valve connected to
scrubber.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 585
Flow and temperature controllers will be provided on process line.
Hydrogenation Plant:
FLP type area will be provided.
Total enclosed process system.
Instrument & Plant Air System.
Nitrogen blanketing in Hydrogenation reactor.
Safety valve and Rupture disc provided on reactor.
Cooling Chilling and power alternative arrangement have been made on reactor.
Hydrogen and Nitrogen Cylinder bank away from the auto clave reactor.
PRV station with shut off valve, safety valve provision will be made for hydrogenation
reaction safety.
Before Hydrogen Gas charging in to reactor and after completion of reaction Nitrogen
flushing will be done.
Flame arrestor will be provided on vent line of reactor and it will be extended up to roof
level.
Open well ventilated and fragile roofs will be provided to on reactor.
Safe Catalyst charging method will be adopted.
SOP will be prepared and operators will be trained for the same.
Static earthing and electric earthing (Double) provided.
Rector vent extended out side the process area and flame arrestor provided on vent line.
Dumping vessel arrangement will be made.
Jumpers for static earthing on pipeline flanges of flammable chemical will be provided.
6.1.4.4.1 PRECAUTIONS DURING STORAGE AND TRANSPORTATION OF HAZARDOUS
CHEMICALS LIQUIDS
Always use the road tankers having authorization for transporting the said liquids.
Vendor will be asked to provide MSDS to Tanker Driver.
Tankers will have clearly marked identification of material being contained with
mentioning Safety Card.
Tanker/truck –Driver contact at gate & ensure meet all points as per Check List
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 586
Driver to have concerned Safety Officer’s contact details to contact him in case of
emergency.
Provide muffler on exhaust while entering tanker within premises.
Ensure Auto Earthling system Boss connection before starting any transferring.
SOP to cover routine checking of Tank farm area to be carried out for checking any
spillage / leakage.
Tanks will be inspected physically daily for having any visual abnormality.
Readings of Temperature & Pressure will be noted, recorded & reported immediately for
abnormality.
Safety instruments like rupture disc, safety valves will be checked at defined duration for
intakeness.
Scheduled testing of tanks to be done for thickness testing.
Tanks to be painted on regular interval defined as per laws to protect them from
atmospheric corrosion.
Barrels to be checked for proper fixing of bungs before sending it outside the premises.
Barrels to be monitored physically daily for developing any pressure or vacuum within it
on long storage.
Concerned persons will be trained properly to use spill kit in case of observing any
spillage inside warehouse.
SOLIDS
Vendor will be asked to provide MSDS to Truck Driver.
Driver to have concerned Safety Officer’s contact details to contact him in case of
emergency.
Provide muffler on exhaust while entering truck within premises.
SOP to cover routine checking of Bags & Containers for checking any damage.
Containers to be tested for safe racking & transportation.
Proper PPE to be used while handling the material & concerned persons to be trained for
usage of the same.
Concerned persons will be trained properly to use spill kit in case of observing any
spillage inside warehouse.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 587
The major hazards in the M/s. Greentec Chemicals Pvt. Ltd. are described below.
Toxic hazard due to leakage of hazardous chemicals from storage tank.
Corrosive hazard due to leakage of chemicals from Carboys.
Electrical hazards due to the electrical major equipment/ machinery, operations,
welding, motors, and heavy lift devices, cabling, human intervention (short circuit
possibility), maintenance work (due to machinery breakdown etc.), plant lighting related
electrical hazards.
Possibility of human injury due to working with mechanical machines, manual handling
etc.
Possibility of injury during chemicals handled, during operations and due to intoxication.
Major dropped objects hazard due to large number of physical handling steps /
operations involved with crane/ overhead lifting/ hoisting equipment.
Fires in any part of the plant working areas – there is a possibility of rapid escalation if it
is not brought under control quickly.
Possibilities of fire hazards at transformers, switchgear and other electrical equipment
etc.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 588
6.1.4.4.2 TRANSPORTATION, UNLOADING AND HANDLING PROCEDURE FOR HAZARDOUS
CHEMICALS
Transportation, Unloading and Handling Procedure for Solvents
SR.
NO.
ACTIVITY TYPE OF POSSIBLE
HAZARD
MITIGATION MEASURES
Leakage& Spillage
Check the source of leakage point.
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Fire & explosion Use water spray to reduce vapors; do not put water
directly on leak, spill area or inside container.
Keep combustibles (wood, paper, oil, etc.) away from
spilled material.
Auto earthling to be connect & ensure
1 Transportation of Solvents by
road tanker
Toxic release Isolate the area
Isolate the container
Training will be provided to driver and cleaner
regarding the safe driving, hazard of Flammable
chemicals, emergency handling.
TREM card will kept with TL.
Fire extinguishers will be kept with TL.
Flame arrestor will be provided to TL exhaust.
Instructions will be given not to stop road tanker in
populated area.
Clear Hazard Identification symbol and emergency
telephone number will be displayed as per HAZCHEM
CODE.
Appropriate PPEs will be kept with TL.
2 Road tanker unloading at tank
farm area
Leakage& Spillage
Check the source of leakage point.
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Auto earthling to be connect & ensure
Fire & explosion Use water spray to reduce vapors; do not put water
directly on leak, spill area or inside container.
Keep combustibles (wood, paper, oil, etc.) away from
spilled material.
Toxic release Isolate the area
Isolate the container
Check the source of leakage point.
Isolate the area
Isolate the container
Spray the water on leakage
Priority will be given to Tanker to immediately enter
the storage premises at site and will not be kept
waiting near the gate or the main road.
Security person will check License, TREM CARD, Fire
extinguisher condition; Antidote Kit, required PPEs as
per SOP laid down.
Store officer will take sample as per sampling SOP from
sampling point.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 589
After approval of QC department unloading procedure
will be allowed be started.
Following precautions will be adopted during unloading
Wheel stopper will be provided to TL at unloading
platform.
Static earthing will be provided to road tanker.
Tanker unloading procedure will be followed according
to check list and implemented.
Flexible SS hose connection will be done at TL outlet
line.
The quantity remaining in the hose pipeline will be
drained to a small underground storage tank.
All TL valves will be closed in TL.
Finally earthing connection and wheel stopper will be
removed.
Only day time unloading will be permitted.
Leakage& Spillage Check the source of leakage point.
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Fire, Explosion Use water spray to reduce vapors; do not put water
directly on leak, spill area or inside container.
Keep combustibles (wood, paper, oil, etc.) away from
spilled material.
3 Storage tank safety
Toxic release. Isolate the area
Isolate the container
Check the source of leakage point.
Isolate the area
Isolate the container
Spray the water on leakage
SS storage tank will be provided as per IS code.
Dyke wall will be provided to storage tank.
Level transmitter will be provided with low level high
level auto cut-off provision.
Vent will be connected to water trap and vent of water
trap will be provided with flame arrestor.
Water sprinkler system will be provided to storage
tank.
Fire hydrant monitor with foam attachment facility will
be provided.
Dumping / Drain vessel/alternate vessel will be
provided to collect dyke wall spillage material.
FLP type pump will be provided.
Nitrogen blanketing will be provided to storage tank.
Double static earthing will be provided to storage tank.
Double Jumper clip will be provided to all Solvent
handling pipeline flanges.
4 Transfer from storage tank to
Day tank
Leakage& Spillage due to
Line rupture, Flange
Gasket failure, Fire,
Explosion, Toxic release.
Double mechanical seal type FLP type pump will be
provided.
Double on / off switch will provided at tank farm and
process area near day tank. Pump auto cut off with day
tank high level will be provided.
Flame arrestor will be provided on day tank vent.
Over flow will be provided for additional safety and it
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 590
will be connected to main storage tank.
NRV will be provided on pump discharge line.
Double Jumper clip will be provided to all solvent
handling pipeline.
Double static earthing will be provided to day tank.
5 Transfer from Day tank to
reactor.
Leakage, Spillage due to
Line rupture, Flange
Gasket failure, Fire,
Explosion, Toxic release.
Gravity transfer.
Total quantity of day tank material will be charged in to
reactor at a time.
NRV will be provided on day tank outlet line.
Static earthing will be provided to storage tank.
Double Jumpers will be provided to pipeline flanges.
Transportation, Unloading and handling procedure for Acrylonitrile (ACN)
SR.NO. ACTIVITY TYPE OF POSSIBLE
HAZARD
MITIGATION MEASURES
1 Road tanker filling
at Kandla /JNPT
/vendor port
& vendor factory
in tank farm area.
Spillage, toxic
release, fire,
explosion.
This activity falls under Kandla/jNPT Port Authority.
Following measures will be provided at Kandla/jNPT Tank
Lorry Filling (TLF) area.
Static earthing provision to Tank Lorry (TL) and
interlocking with filling pump.
Wheel stoppers to TL.
Automatic Charging by PLC based system with volume
measurement.
Flame arrestor/ spark arrestor on TL exhaust.
2 Transportation of
ACN by road
tanker
Leakage & Spillage
Fire, explosion,
Toxic release
Check the source of leakage point.
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Use water spray to reduce vapors; do not put water
directly on leak, spill area or inside container.
Keep combustibles (wood, paper, oil, etc.) away from
spilled material.
Isolate the area
Isolate the container
Training will be provided to driver and cleaner regarding
the safe driving, hazard of ACN, ACN emergency handling,
use of antidote kit administration.
TREM card will kept with TL.
Antidote Kit will be kept with TL.
SCBA set will be kept with TL.
Fire extinguishers will be kept with TL.
All the TL will be equipped with Global Positioning system
(GPS) and route will be predefined.
Flame arrestor will be provided to TL exhaust.
Instructions will be given not to stop ACN road tanker in
populated area.
Clear Hazard Identification symbol and emergency
telephone number will be displayed as per HAZCHEM
CODE.
Appropriate PPEs will be kept with TL.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 591
3 ACN tank Lorry
unloading at site
Leakage& Spillage,
Fire, explosion,
Toxic release
Check the source of leakage point.
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Use water spray to reduce vapors; do not put water
directly on leak, spill area or inside container.
Keep combustibles (wood, paper, oil, etc.) away from
spilled material.
Isolate the area
Isolate the container
Priority will be given to Tanker to immediately enter the
storage premises at site and will not be kept waiting near
the gate or the main road.
Security person will check License, TREM CARD, Fire
extinguisher condition; SCBA set condition, Antidote Kit,
required PPEs as per SOP laid down.
Store officer will take sample as per sampling SOP from
sampling point.
After approval of QC department unloading procedure will
be allowed be started.
Following precautions will be adopted during unloading by
Nitrogen pressure.
Wheel stopper will be provided to TL at unloading
platform.
Static earthing will be provided to road tanker.
Tanker unloading procedure will be followed according to
check list and implemented.
Nitrogen hose connection will be done with TL nitrogen
inlet line for ACN transfer by Nitrogen pressure.
Flexible SS hose connection will be done at TL outlet line.
After connecting all hoses properly, check will be carried
out for leakage and then charging line valve will be
opened, followed by TL outlet line valve and finally
Nitrogen charging line valve will be opened gradually to
apply N2 pressure inside TL.
When TL is empty, first N2 pressure line valve will be
closed followed by TL outlet line valve and finally tank
charging line valve.
The quantity remaining in the hose pipeline will be
drained to a small underground storage tank, which will
be subsequently transferred by nitrogen pressure to the
main storage tank thus ensuring complete closed
conditions for ACN transfer from road tanker.
All TL valves will be closed keeping nitrogen blanketing in
TL.
Finally earthing connection and wheel stopper will be
removed.
Only day time unloading will be permitted.
Following precautions will be adopted during TL unloading
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 592
work by pump.
Wheel stopper will be provided to TL at unloading plate
form.
Static earthing will be provided to road tanker.
Tanker unloading procedure with check list will be
followed and implemented.
Flexible SS hose connection will be made to TL outlet line.
After connecting all hoses will be properly checked for any
leakages and then storage tank charging line valve will be
opened followed by TL outlet line valve and finally pump
will be started.
When TL is empty, stop the pump then tank charging line
valve is closed followed by TL outlet line valve.
The quantity remaining in the hose pipeline will be
drained to a small underground storage tank, which will
be subsequently transferred by nitrogen pressure to the
main storage tank thus ensuring complete closed
conditions for ACN transfer from road tanker.
All TL valves are closed and nitrogen blanketing in TL will
be provided.
Earthing connection and wheel stopper will be removed.
Only day time unloading will be permitted.
4 Storage tank
safety
Leakage &Spillage,
Fire, Explosion,
Toxic release
Check the source of leakage point.
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Use water spray to reduce vapors; do not put water
directly on leak, spill area or inside container.
Keep combustibles (wood, paper, oil, etc.) away from
spilled material.
Isolate the area
Isolate the container
SS storage tank will be provided as per IS code.
Dyke wall will be provided to storage tank.
Level transmitter will be provided with low level high level
auto cut-off provision.
Vent will be connected to water trap and vent of water
trap will be provided with flame arrestor.
Water sprinkler system will be provided to storage tank.
Fire hydrant monitor with foam attachment facility will be
provided.
Dumping / Drain vessel will be provided to collect dyke
wall spillage material.
FLP type pump will be provided.
Nitrogen blanketing will be provided to storage tank.
Double static earthing will be provided to storage tank.
Double Jumper clip will be provided to all ACN handling
pipeline flanges.
5 ACN transfer from
storage tank to
Leakage, Spillage
due to Line
Double mechanical seal type FLP type pump will be
provided.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 593
Day tank rupture, Flange
Gasket failure,
Fire, Explosion,
Toxic release.
Double on / off switch will provided at tank farm and
process area near day tank. Pump auto cut off with day
tank high level will be provided.
Flame arrestor will be provided on day tank vent.
Over flow will be provided for additional safety and it will
be connected to main storage tank.
NRV will be provided on pump discharge line.
Double Jumper clip will be provided to all ACN handling
pipeline.
Double static earthing will be provided to day tank.
6 ACN transfer from
Day tank to
reactor.
Leakage, Spillage
due to Line
rupture, Flange
Gasket failure,
Fire, Explosion,
Toxic release.
Gravity transfer.
Total quantity of day tank material will be charged in to
reactor at a time.
NRV will be provided on day tank outlet line.
Static earthing will be provided to storage tank.
Double Jumpers will be provided to pipeline flanges.
Bromine Transportation, Unloading and handling Procedure:
SR.NO. ACTIVITY TYPE OF POSSIBLE
HAZARD
MITIGATION MEASURES
1 Transportation of
Bromine by ISO
container
Leakage, Spillage,
Toxic release
Leak check with ammonia torch and detect the leak point.
ELIMINATE all ignition sources (no smoking, flares, sparks
or flames in immediate area).
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Prevent entry into waterways, sewers, basements or
confined areas.
Absorb or cover with dry earth, sand or other non-
combustible material and transfer to containers.
Do not get water inside containers.
GPS will be installed in all the trucks and ISO container
vehicle.
Driver and assistant will be trained in using GPS.
Open space separated from public highway and public
dwellings, where public does not normally pass. No
passengers are allowed.
The crew shall know how to use fire-fighting appliances.
The driver or driver's assistant may not open a package
containing bromine.
Bromine receptacles are not to be checked with open
flames.
No smoking is permitted around the transport unit or in
the vicinity of the vehicle during handling operations.
The engine is to be shut off during all handling operations
unless required to drive pumps, hoist, etc.
Parking brakes are to be applied whenever parked.
If the vehicle is parked on a road at night or with poor
visibility, warning signs are to be placed 10 meters ahead
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 594
of and behind the vehicle.
TREM CARD provided to all transporters and trained for
transportation Emergency of Hazardous chemicals.
All trucks having 1 kg Sodium Thiosulphate bag.
Training will be provided to driver and cleaner regarding
the safe driving, hazard of Bromine emergency handling,
use of SCBA sets and neutralizing agent.
SCBA set will be kept with ISO container truck.
All the ISO container truck will be equipped with Global
Positioning system (GPS) and route will be predefined.
Clear Hazard Identification symbol and emergency
telephone number will be displayed as per HAZCHEM
CODE.
Appropriate PPEs will be kept with Truck.
3 Bromine ISO
container loading
and handling at
site
Leakage, Spillage,
toxic release
Leak check with ammonia torch and detect the leak point.
ELIMINATE all ignition sources (no smoking, flares, sparks
or flames in immediate area).
Do not touch damaged containers or spilled material
unless wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Prevent entry into waterways, sewers, basements or
confined areas.
Absorb or cover with dry earth, sand or other non-
combustible material and transfer to containers.
Do not get water inside containers.
Directly ISO container will be placed at storage area and
connected with process tank.
Wear recommended personal protective equipment
during connection of ISO container.
Make sure the absorber unit is working and capable of
handling vented bromine fumes.
BE SURE THAT DRY AIR (DEW POINT -40"C) OR DRY
NITROGEN is available in ample supply and its pressure is
controlled below 3 atm. gauge.
Check that all the Iso-container valves are closed and blind
flanges are in place.
Remove the blind flange above the red valve.
Connect your pressure release line to the red valve outlet.
Use a new rubber gasket (use limit - 24 hours) to ensure
tight connection.
Open the red valve slowly and then the depressurizing
valve, to release any pressure which might have
developed in the Iso-container.
Remove the blind flange above the yellow valve.
Connect your line to the yellow valve outlet. Use a new
rubber gasket (use limit - 24 hours) to ensure tight
connection.
Open the yellow valve and all the valves in your liquid
unloading line.
Close the depressurizing valve.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 595
Open the pressurizing valve, at first slowly (to check for
bromine leaks), then fully, to start bromine unloading. Use
only enough pressure to lift the bromine to the high point
in the unloading system.
NEVER EXCEED 3 ATM. PRESSURE
When air/nitrogen blows through the unloading line into
your storage tank, the Iso-container is empty.
Close the pressurizing valve.
Close the yellow valve and then all the other valves in your
liquid unloading line.
Slowly open the depressurizing valve to release the
air/nitrogen pressure on the Iso-container to your
absorber unit. Wait 5 minutes.
Close the red valve and then the depressurizing valve.
Cautiously disconnect your liquid unloading line from the
yellow valve of the Iso-container. Replace its blind flange,
tightening all the bolts. Do not forget to reinstall the
proper gasket.
Disconnect your pressure release line from the red valve
of the Iso-container. Replace its blind flange, tightening all
the bolts. Do not forget to reinstall the proper gasket.
If there has been a bromine spillage, wash it off the Iso-
container with plenty of water to prevent corrosion. Small
bromine spills on the ground may be neutralized with a
clear soda ash or a sodium thiosulphate solution. Then
dispose of in a manner approved by the local authorities.
Close the cover dome and pin it securely.
Mark the Iso-container EMPTY (use erasable means).
Bromine Iso tanks should be stored no closer than 10
meters from human or animal consumable articles.
Explosives and flammable materials should not be stored
close to bromine.
There would be sufficient bromine storage tank capacity
or an empty ISO tank to accommodate the transfer of
bromine from a leaking container
Area where bromine will be used or stored will be
enclosed so that unauthorized persons and animals are
prevented from entering the area. Adequate lighting will
be provided to allow sufficient night surveillance.
Surveillance will be provided 24 hours a day.
Personnel escape routes will be clearly marked and it will
be maintained without any obstructions including
adequately sized doors and windows.
Facilities like offices, eating, showering and changing
rooms, will be located in up wind direction and remote
from the area where bromine is handled or stored.
Provide an adequate supply of clean water for washing
and showers.
Emergency siren, telephone will be provided in storage
area for the reporting of accidents or emergency
situations. The emergency telephone numbers will be
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 596
displayed at prominent locations and it include the fire
department, ambulance service, emergency response
team, hospital and police.
A wind sock will be provided which will clearly visible from
all points on the site and replaced as required. This is
required for indicating wind strength and direction.
Emergency respirator equipment cabinets (Cupboard) will
be installed not more than 30 meters or ten seconds
walking distance from any location in the storage area.
Showers and eyewash fountains will be provided, clearly
marked, well lit and with unobstructed access.
Signs will be posted prominently at the site entrance and
throughout the installation with area maps showing
access ways, hydrant locations, emergency showers,
location of emergency equipment and emergency
telephone numbers.
All management and operating personnel involved in the
use or handling of bromine will undergo safety training, in
addition to specific task training.
Only experienced well-trained operators will be allowed to
receive and unload bromine receptacles.
The management will ensure that emergency response
plans have been made and coordinated with the
emergency response local authorities.
Safety permit for hazardous material loading unloading
will be prepared and implemented.
Fire hydrant system and water sprinkler system installed
at tank farm area.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 597
Chlorine Transportation, Unloading and handling Procedure:
SR.NO. ACTIVITY TYPE OF POSSIBLE
HAZARD
MITIGATION MEASURES
1 Transportation of
Chlorine Tonners
by road tanker
Leakage, Spillage,
Toxic release
Leak check with ammonia torch and detect the leak point.
ELIMINATE all ignition sources (no smoking, flares, sparks or
flames in immediate area).
Do not touch damaged containers or spilled material unless
wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Prevent entry into waterways, sewers, basements or
confined areas.
Absorb or cover with dry earth, sand or other non-
combustible material and transfer to containers.
Do not get water inside containers.
Training will be provided to driver and cleaner regarding the
safe driving, hazard of Chlorine emergency handling, use of
SCBA sets.
TREM card will kept with TL.
SCBA set will be kept with TL.
Instructions will be given not to stop Chlorine road truck in
populated area.
Clear Hazard Identification symbol and emergency
telephone number will be displayed as per HAZCHEM CODE.
Appropriate PPEs will be kept with TL.
2 Chlorine tonners
unloading at site
Leakage, Spillage,
toxic release
Leak check with ammonia torch and detect the leak point.
ELIMINATE all ignition sources (no smoking, flares, sparks or
flames in immediate area).
Do not touch damaged containers or spilled material unless
wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Prevent entry into waterways, sewers, basements or
confined areas.
Absorb or cover with dry earth, sand or other non-
combustible material and transfer to containers.
Do not get water inside containers.
Priority will be given to Tanker to immediately enter the
storage premises at site and will not be kept waiting near
the gate or the main road.
Security person will check License, TREM CARD, Fire
extinguisher condition; SCBA set condition, required PPEs as
per SOP laid down.
3 Chlorine tonners
storage shed
Leakage, Spillage,
Toxic release.
Leak check with ammonia torch and detect the leak point.
ELIMINATE all ignition sources (no smoking, flares, sparks or
flames in immediate area).
Do not touch damaged containers or spilled material unless
wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Prevent entry into waterways, sewers, basements or
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confined areas.
Absorb or cover with dry earth, sand or other non-
combustible material and transfer to containers.
Do not get water inside containers.
SOP will be prepared for safe handling of Chlorine toners.
Chlorine Emergency Kit will be procured and kept ready at
chlorine shed.
Chlorine Hood with blower will be provided with scrubbing
arrangement.
Safety Shower and eye wash will be provided in Chlorine
shed area.
Tonner handling EOT crane will be installed in Chlorine shed
area for safe tonner handling.
Safety Valve will be provided on chlorine header line and it
will be connected to caustic scrubber.
SCBA sets will be kept ready at chlorine handling area.
Safety valve will be provided on vaporizer header and outlet
of safety valve connected to scrubber.
Flow and temperature controllers will be provided on
process line.
4 Chlorine tonners
connected with
header
Leakage, Spillage
due to Line
rupture, Toxic
release.
Leak check with ammonia torch and detect the leak point.
ELIMINATE all ignition sources (no smoking, flares, sparks or
flames in immediate area).
Do not touch damaged containers or spilled material unless
wearing appropriate protective clothing.
Stop leak if you can do it without risk.
Prevent entry into waterways, sewers, basements or
confined areas.
Absorb or cover with dry earth, sand or other non-
combustible material and transfer to containers.
Do not get water inside containers.
Teflon or copper tube will be used for connection with
header.
Pressure gauge and safety valve will be provided on header
line.
Transportation, Unloading and handling procedure for Phenol:
SR.NO. ACTIVITY TYPE OF POSSIBLE
HAZARD
MITIGATION MEASURES
1 Transportation of
Phenol by road
tanker
Leakage, Spillage,
Toxic release
Training will be provided to driver and cleaner regarding
the safe driving, hazard of Flammable chemicals,
emergency handling, and use of SCBA sets
administration.
TREM card will kept with TL.
Instructions will be given not to stop road tanker in
populated area.
Clear Hazard Identification symbol and emergency
telephone number will be displayed as per HAZCHEM
CODE.
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Appropriate PPEs will be kept with TL.
Emergency telephone numbers list for OFF site
emergency agencies will be provided in TREM CARD.
2 Phenol Road tanker
unloading at site.
Leakage, Spillage,
toxic release, fire
Priority will be given to Tanker to immediately enter the
storage premises at site and will not be kept waiting
near the gate or the main road.
Security person will check License, TREM CARD, Fire
extinguisher condition, required PPEs as per SOP laid
down.
Store officer will take sample as per sampling SOP from
sampling point.
After approval of QC department unloading procedure
will be allowed be started.
Following precautions will be adopted during unloading
Wheel stopper will be provided to TL at unloading
platform.
Tanker unloading procedure will be followed according
to check list and implemented.
Flexible hose connection will be done at TL outlet line
and checked for no leakage.
Every time rubber gasket will be changed.
The quantity remaining in the hose pipeline will be
drained to a small container, which will be subsequently
transferred to the main storage tank thus ensuring
complete closed conditions for transfer from road
tanker.
3 Phenol Storage
tank safety
Leakage, Spillage,
Toxic release.
Storage tank will be stored away from the process plant
in tank farm area.
Caution note and emergency handling procedure will be
displayed at unloading area and trained all operators.
NFPA label will be provided.
Required PPEs like full body protection PVC apron, Hand
gloves, gumboot, Respiratory mask etc. will be provided
to operator.
Safety shower, eye wash with quenching unit will be
provided in acid storage area.
Material will be handled in close condition in pipe line.
Dyke wall will be provided, collection pit with valve
provision.
Jacketed tank will be provided and steam heating will be
provided in jacket.
Double drain valve will provided.
Level gauge will be provided on storage tank.
Safety permit for loading unloading of hazardous
material will be prepared and implemented.
Fire hydrant system with jockey pump as per TAC norms
will be installed.
4 Phenol transferred
from storage tank
to Day tank
Leakage, Spillage
due to Line
rupture, Flange
Double mechanical seal type pump will be provided.
Over flow will be provided for additional safety and it
will be connected to main storage tank.
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Gasket failure,
Toxic release.
NRV will be provided on pump discharge line.
Flange Guard will be provided to all flanges.
5 Phenol transfer
from Day tank to
reactor.
Leakage, Spillage
due to Line
rupture, Flange
Gasket failure,
Toxic release.
Gravity transfer.
Double valve will be installed on day tank outlet line.
Total quantity of day tank material will be charged in to
reactor at a time.
Flange guard will be provided to pipeline flanges.
6.1.5 CONSEQUENCE ANALYSIS
In a plant handling hazardous chemicals, the main hazard arises due to storage, handling &
use of these chemicals. If these chemicals are released into the atmosphere, they may cause
damage due to resulting fires or vapour clouds. Blast Overpressures depend upon the
reactivity class of material between two explosive limits.
Operating Parameters
Potential vapour release for the same material depends significantly on the operating
conditions. Especially for any liquefied gas, the operating conditions are very critical to
assess the damage potential. If we take up an example of ammonia, if it is stored at ambient
temperature, say 30oC, and then the vapour release potential of the inventory is much
higher as compared to the case if it is stored at 0oC.
Inventory
Inventory Analysis is commonly used in understanding the relative hazards and short listing
of release scenarios. Inventory plays an important role in regard to the potential hazard.
Larger the inventory of a vessel or a system, larger the quantity of potential release. The
potential vapour release (source strength) depends upon the quantity of liquid release, the
properties of the materials and the operating conditions (pressure, temperature). If all
these influencing parameters are combined into a matrix and vapour source strength
estimated for each release case, a ranking should become a credible exercise.
Loss of Containment
Plant inventory can get discharged to Environment due to Loss of Containment. Certain
features of materials to be handled at the plant need to the clearly understood to firstly list
out all significant release cases and then to short list release scenarios for a detailed
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examination. Liquid release can be either instantaneous or continuous. Failure of a vessel
leading to an instantaneous outflow assumes the sudden appearance of such a major crack
that practically all of the contents above the crack shall be released in a very short time. The
more likely event is the case of liquid release from a hole in a pipe connected to the vessel.
The flow rate is depending on the size of the hole as well as on the pressure, which was
present, in front of the hole, prior to the accident. Such pressure is basically dependent on
the pressure in the vessel. The vaporisation of released liquid depends on the vapour
pressure and weather conditions. Such consideration and others have been kept in mind
both during the initial listing as well as during the short listing procedure. In the study,
Maximum Credible Loss accident methodology is to be used, therefore, the largest potential
hazard inventories have been considered for consequence estimation.
6.1.5.1 DAMAGE CRITERIA
In consequence analysis, use is made of a number of calculation models to estimate the
physical effects of an accident (spill of hazardous material) and to predict the damage
(lethality, injury, material destruction) of the effects. The calculations can roughly be divided
in three major groups:
a) Determination of the source strength parameters;
b) Determination of the consequential effects;
c) Determination of the damage or damage distances.
The basic physical effect models consist of the following.
Source strength parameters
* Calculation of the outflow of liquid, vapour or gas out of a vessel or a pipe, in case of
rupture. Also two-phase outflow can be calculated.
* Calculation, in case of liquid outflow, of the instantaneous flash evaporation and of
the dimensions of the remaining liquid pool.
* Calculation of the evaporation rate, as a function of volatility of the material, pool
dimensions and wind velocity.
* Source strength equals pump capacities, etc. in some cases.
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Consequential effects
* Dispersion of gaseous material in the atmosphere as a function of source strength,
relative density of the gas, weather conditions and topographical situation of the
surrounding area.
* Intensity of heat radiation [in kW/ m2] due to a fire or a BLEVE, as a function of the
distance to the source.
* Energy of vapour cloud explosions [in N/m2], as a function of the distance to the
distance of the exploding cloud.
* Concentration of gaseous material in the atmosphere, due to the dispersion of
evaporated chemical. The latter can be either explosive or toxic.
It may be obvious, that the types of models that must be used in a specific risk study
strongly depend upon the type of material involved:
- Gas, vapour, liquid, solid
- Inflammable, explosive, toxic, toxic combustion products
- Stored at high/low temperatures or pressure
- Controlled outflow (pump capacity) or catastrophic failure?
Selection of Damage Criteria
The damage criteria give the relation between extent of the physical effects (exposure) and
the percentage of the people that will be killed or injured due to those effects. The
knowledge about these relations depends strongly on the nature of the exposure. For
instance, much more is known about the damage caused by heat radiation, than about the
damage due to toxic exposure, and for these toxic effects, the knowledge differs strongly
between different materials.
In Consequence Analysis studies, in principle three types of exposure to hazardous effects
are distinguished:
1. Heat radiation, from a jet, pool fire, a flash fire or a BLEVE.
2. Explosion
3. Toxic effects, from toxic materials or toxic combustion products.
In the next three paragraphs, the chosen damage criteria are given and explained.
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Heat Radiation
The consequence caused by exposure to heat radiation is a function of:
The radiation energy onto the human body [kW/m2];
The exposure duration [sec];
The protection of the skin tissue (clothed or naked body).
The limits for 1% of the exposed people to be killed due to heat radiation, and for
second-degree burns are given in the table herein:
Damages to Human Life Due to Heat Radiation
Exposure
Duration
Radiation for
1% lethality
(KW/m2)
Radiation for 2nd
degree burns
(KW/m2)
Radiation for
first degree
burns (KW/m2)
10 Sec 21.2 16 12.5
30 Sec 9.3 7.0 4.0
Since in practical situations, only the own employees will be exposed to heat radiation in
case of a fire, it is reasonable to assume the protection by clothing. It can be assumed that
people would be able to find a cover or a shield against thermal radiation in 10 sec. time.
Furthermore, 100% lethality may be assumed for all people suffering from direct contact
with flames, such as the pool fire, a flash fire or a jet flame. The effects due to relatively
lesser incident radiation intensity are given below.
Effects Due To Incident Radiation Intensity
INCIDENT
RADIATION
KW/m2
TYPE OF DAMAGE
0.7 Equivalent to Solar Radiation
1.6 No discomfort for long exposure
4.0 Sufficient to cause pain within 20 sec. Blistering of skin (first degree burns are likely)
9.5 Pain threshold reached after 8 sec. second degree burns after 20 sec.
12.5 Minimum energy required for piloted ignition of wood, melting plastic tubing etc.
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Explosion
In case of vapour cloud explosion, two physical effects may occur:
* a flash fire over the whole length of the explosive gas cloud;
* a blast wave, with typical peak overpressures circular around ignition source.
As explained above, 100% lethality is assumed for all people who are present within the
cloud proper.
For the blast wave, the lethality criterion is based on:
* A peak overpressure of 0.1 bar will cause serious damage to 10% of the
housing/structures.
* Falling fragments will kill one of each eight persons in the destroyed buildings.
The following damage criteria may be distinguished with respect to the peak overpressures
resulting from a blast wave:
Damage Due To Overpressures
Peak Overpressure Damage Type
0.83 bar Total Destruction
0.30 bar Heavy Damage
0.10 bar
0.03 bar
Moderate Damage
Significant Damage
0.01 bar Minor Damage
From this it may be concluded that p = 0.17 E+5 pa corresponds approximately with 1%
lethality. Furthermore it is assumed that everyone inside an area in which the peak
overpressure is greater than 0.17 E+ 5 pa will be wounded by mechanical damage. For the
gas cloud explosion this will be inside a circle with the ignition source as its centre.
Intoxication
The consequences from inhalation of a toxic vapour/gas are determined by the toxic dose.
This dose D is basically determined by:
- Concentration of the vapour in air;
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- Exposure duration.
Furthermore, of course, the breathing rates of the victim, as well as the specific toxic
mechanism unto the metabolism play an important role.
The dose is defined as D = Cn.t, with:
C = concentration of the toxic vapour, in [ppm] or [mg/m3];
t = exposure duration, in [sec] or [min];
n = exponent, mostly > 1.0; this exponent takes into account the fact that a high
concentration over a short period results in more serious injury than a low
concentration over a relatively longer period of exposure. The value of n
should be greater than zero but less than 5.
The given definition for D only holds if the concentration is more or less constant over the
exposure time; this may be the case for a (semi) continuous source. In case of an
instantaneous source, the concentration varies with time; the dose D must be calculated
with an integral equation:
D = Cn.dt
For a number of toxic materials, so-called Vulnerability Models (V.M.) has been developed.
The general equation for a V.M. (probit function) is:
Pr = a + b.ln (Cn.t), with
Pr = probit number, being a representation of the percentage of people suffering
a certain kind of damage, for instance lethality
Pr = 2.67 means 1% of the population;
Pr = 5.00 means 50% of the population;
a and b material dependent numbers;
Cn.t = dose D, as explained above.
The values for a and b are mostly derived from experiments with animals; occasionally,
however, also human toxicity factors have been derived from accidents in past. In case only
animal experiments are available, the inhalation experiments with rats seem to be best
applicable for predicting the damage to people from acute intoxication. Although much
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research in this field have been done over the past decades, only for a limited number of
toxic materials consequence models have been developed. Often only quite scarce
information is available to predict the damage from an acute toxic exposition. Data
transformation from oral intoxication data to inhalation toxicity criteria is sometimes
necessary. Generally, in safety evaluations pessimistic assumptions are applied in these
transformation calculations. The calculated damage (distance) may be regarded as a
maximum. For the purposes of a response to a major incident, the IDLH value level has been
chosen for the ‘wounded‘criteria. This type of injury will require medical attention.
6.1.5.2 MAXIMUM CREDIBLE LOSS ACCIDENT SCENARIOS
A Maximum Credible Accident (MCA) can be characterised as the worst credible accident. In
other words: an accident in an activity, resulting in the maximum consequence distance that
is still believed to be possible. A MCA-analysis does not include a quantification of the
probability of occurrence of the accident. Another aspect, in which the pessimistic approach
of MCA studies appears, is the atmospheric condition that is used for dispersion
calculations. As per the reference of the study, weather conditions having an average wind
speed of 2.05 m/s have been chosen.
The Maximum Credible Loss (MCL) scenarios have been developed for the Facility. The MCL
cases considered, attempt to include the worst “Credible” incidents- what constitutes a
credible incident is always subjective. Nevertheless, guidelines have evolved over the years
and based on basic engineering judgement, the cases have been found to be credible and
modelling for assessing vulnerability zones is prepared accordingly. Only catastrophic cases
have been considered and not partial or small failures (as is the case in Quantitative Risk
Assessment where contributions from low frequency - high outcome effect as well as high
frequency - low outcome events are distinguished). The objective of the study is emergency
planning, hence only holistic & conservative assumptions are used for obvious reasons.
Hence though the outcomes may look pessimistic, the planning for emergency concept
should be borne in mind whilst interpreting the results.
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6.1.5.2.1 CONSEQUENCE ANALYSIS CALCULATIONS
The Consequence Analysis has been done for selected scenarios. This has been done for
weather conditions having wind speed 2.05 m/s. In Consequence Analysis, geographical
location of the source of potential release plays an important role. Consideration of a large
number of scenarios in the same geographical location serves little purpose if the dominant
scenario has been identified and duly considered.
6.1.5.2.2 SOFTWARE USED FOR CALCULATIONS
PHAST MICRO: Phast is the most comprehensive software available for performing Process
Hazard Analysis (PHA), Quantitative Risk Assessment (QRA) and Financial Risk Analysis (FRA).
Our extensively validated software for consequence and risk assessment is used by
governments and industry helping them to comply with local safety regulation and their
own corporate best practice. Phast contains all the discharge, dispersion, effects and risk
models you will need to accurately assess all your major hazards and associated risks. Phast
Consequence provides you with comprehensive hazard analysis facilities to examine the
progress of a potential incident from the initial release to its far-field effects.
TOXIC AND FLAMMABLE IMPACT
It calculates the initial discharge, as the material expands from its storage conditions to
atmospheric, through dispersion, as the material mixes with air and dilutes, and the
subsequent toxic or flammable effects. Phast includes a wide range of models for discharge
and dispersion as well as flammable, explosive and toxic effects.
DISCHARGE
Phast requires basic information about storage or process conditions and material
properties in order to perform discharge calculations
The software comes with an integrated material property database containing more
than 1,600 pre-defined pure component chemicals
Various discharge scenario options have been implemented to represent common
process failures, and model their behaviour. These include:
Leaks and line ruptures from long & short pipelines
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Catastrophic ruptures
Relief valve and disc ruptures
Tank roof collapse
Vent from vapour spaces
In building release effects
DISPERSION
The dispersion models within Phast are able to model the following phenomena
Dispersion of gas, liquid and two-phase releases
Liquid droplet thermo dynamics calculations and liquid droplet rainout
Pool spreading and vaporization
Building wake dispersion effects for vapour releases
FLAMMABLE EFFECTS
For releases of flammable material Phast calculates
Radiation profiles and contours from a range of fire scenarios including pool fires,
flash fires, jet fires and fire balls, including cross-wind effects on a jet fire
Vapour Cloud Explosion modeling using industry standards models including the
TNO Multi-energy, Baker Strehlow Tang and TNT Equivalence models
Overpressure contours from Boiling Liquid Expanding Vapour Explosions
TOXIC EFFECTS
Graphs of toxic concentration profile
Indoor and outdoor toxic dose prediction
Reporting of distance to specific dose and concentration
Calculated exposure time and use as “averaging time” for passive dispersion effects
PHAST RISK
Phast Risk allows you to combine the flammable and toxic consequences from each
scenario in your QRA model with their likelihood to quantify the risk of fatalities. Phast Risk
allows you to take account of local population distribution, sources of ignition, land usage
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and local prevailing weather conditions. It is designed to perform all the analysis, data
handling and results presentation elements of a QRA within a structured framework.
Phast Risk allows you to quickly identify major risk contributors so that time and efforts can
be directed to mitigating these highest risk activities. Based on effects calculations and
population vulnerabilities, Phast Risk can integrate over all scenarios and weather
conditions to estimate the total risk. The established individual and societal risk indicators
are predicted by Phast Risk across your facility and surrounding area using the classical QRA
methodology. Risk ranking reports can be produced at points of strategic importance to
show the relative influence of the various failure scenarios and their contribution to both
the individual and societal risk metrics.
A key benefit of Phast Risk is the ability to identify major risk contributors and differentiate
these from incidents with worst case consequences which might otherwise dominate the
safety reviews. Whilst medium scale incidents have lesser consequences, they may have a
higher frequency, which, when combined with their hazardous effects, generate a higher
level of risk. Time and effort directed to mitigating high consequence but often low
frequency events may not be well spent. Phast Risk helps you direct this effort more
effectively. Phast Risk also provides facilities to help you manage large quantities of input
data, including scenarios, parameters, wind roses, ignition and population, and combine
these in many ways. This is critical when looking at sensitivity analyses and assessing the
merits of a range of risk reduction measures.
Benefits
Facilitates cost reduction in terms of losses and insurance
Allows optimization of plant and process design
Assist in compliance with safety regulators
Enables quicker response to hazardous incidents
Improve engineer’s understanding of potential hazards
Regular software upgrades incorporate industry experience and expertise, and
advances in consequence modeling technology
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6.1.5.2.3 SCENARIOS
TABLE – 6.4
POSSIBLE ACCIDENT SCENARIOS
Scenario MCL Scenario Pressure & Temp. Quantity
1 Release of Chlorine Liquefied
@ RT 10 kg/cm2
27 MT
2 Release of Hydrogen NTP 3000 Kg
3 Release of Xylene NTP 15 MT
4 Release of Toluene NTP 17 KL
5 Release of Methanol NTP 25 KL
6 Release of Ethanol NTP 25 KL
7 Release of Hydrochloric Acid NTP 10 KL
8 Release of Iso Propyl Alcohol NTP 12 KL
9 Release of Phenol NTP 25 KL
10 Release of Nitric Acid NTP 15 KL
11 Release of Liq. Ammonia NTP 700 kg
12 Release of Methylene Dichloride NTP 20 KL
13 Release of Ethylene Dichloride NTP 20 KL
14 Release of Acetic Anhydride NTP 40 KL
15 Release of Sulphuric Acid NTP 20 KL
16 Release of Bromine NTP 12 MT
17 Release of Ethyl Acetate NTP 20 KL
18 Release of Hexane NTP 4 KL
19 Release of THF NTP 4 KL
20 Release of CS2 NTP 150 KL
21 Release of EDA NTP 250 KL
22 Release of PCl3 @1kg/Cm2 N2 Pr 150 KL
23 Unconfined Pool Fire Simulations for Drum Storage
Area
NTP 200 Lit x 100
Drums
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Scenario – 1 Release of Chlorine
This scenario considers release of Chlorine from Storage Tank:
Results indicate:
Puff Isopleth Simulation for Chlorine Tonner Catastrophic Failure
Scenario : PUFF DISPERSION
In put Data
Stored quantity 900 Kg X 30 Cylinders =27 MT
Instantaneous Puff Release quantity 900 Kgs.
Hazard Level Concentration (PPM) Ground level distance (Meter)
Lc50 1017 211
IDLH 10 856
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Point source plume release for Chlorine toner liquid/ gas phase valve failure
Scenario : POINT SOURCE PLUME RELEASE
In put Data
Stored quantity 900 Kgs
Rate of release 1000 g/s
Hazard Level Concentration (PPM) Ground level distance (Meter)
Lc50 1017 166
IDLH 10 555
TWA/ TLV 1.00 1045
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Measures to control and mitigate Emergency of Chlorine:
Evacuate the area in down wind direction:
For Chlorine evacuate area in down wind direction up to 0.4 km (400 meter) in small spillage and in case of
large spillage, evacuate the area in down wind direction 3.5 kms (3500 meters).
SOP will be prepared for safe handling of Chlorine tonners.
Tonner handling EOT crane will be installed in Chlorine shed area for safe tonner handling.
Safety Valve will be provided on chlorine header line and it will be connected to caustic scrubber.
Safety valve will be provided on vaporizer header and outlet of safety valve connected to scrubber.
Flow and temperature controllers will be provided on process line.
Chlorine Gas detectors will be provided in Chlorine shed and near Header.
Scenario base On Site emergency Plan will be prepared.
Mitigation measures to control Emergency:
Chlorine Emergency Kit will be procured and kept ready at chlorine shed.
Chlorine Hood with blower will be provided with scrubbing arrangement.
SCBA sets will be kept ready at chlorine handling area.
Safety Shower and eye wash will be provided in Chlorine shed area.
Chlorine absorption system will be provided. In case of chlorine leakage in chlorine shed it will be suck
through blower and it will be scrubbed in Caustic scrubber.
Emergency siren and wind sock will be provided.
Tele Communication system and mobile phone will be used in case of emergency situations for
communication.
First Aid Boxes and Occupational health centre will be made at site.
Emergency organization and team will be prepared as per on site-Off site emergency planning.
Full body protection suite and other PPEs will be kept ready in ECC at site.
Emergency team will be prepared and trained for scenario base emergency. Like Toxic control team,
Fire control team, First aid team, Communication and general administration team, Medical team etc.
EMERGENCY RESPONSE
EMERGENCY RESPONSE
SPILL OR LEAK
· Fully encapsulating, vapor protective clothing should be worn for spills and leaks with no fire.
· Do not touch or walk through spilled material.
· Keep combustibles (wood, paper, oil, etc.) away from spilled material.
· Stop leak if you can do it without risk.
· Use water spray to reduce vapors or divert vapor cloud drift. Avoid allowing water runoff to contact spilled
material.
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Scenario – 2 Release of Hydrogen
This scenario considers release of Hydrogen from Storage Tank:
Results indicate:
Scenario: Diffusion Jet Fire Simulation for 1.0 cm copper connecting pipe to PRV station
In put Data Results of Computations
Stored quantity Cylinder bank Max. IHR at flame centre height 52.49 Kw/m2
Gas Jet diameter 1 (cm) Flame centre height 63 meter
Gas velocity in the
leakage hole/ pipe
143463 m/s Maximum Flame width 12 meter
Wind speed 2.05 m/s Heat Flux 8.5 KW/ m2
Gas Density 0.067 kg/m3 Flame Surface Area 3778 m
2
Incident Intensity of Heat
Radiation ( IHR) at
ground level KW /m 2
IHR- Isopleth
Distance
( Meters )
Effect if IHR at Height of Simulation
37.5 8.3 Damage to process equipment. 100 % Fatal in 1 Min. 1 % fatal in 10
sec.
12.5 14.4 Min. to ignite wood (with flame contact). 1 % fatal in 1 min. 1st
deg.
burn in 10 sec.
4.0 25.4 Pain after 20 secs. Blistering unlikely.
Results
In the 8.3 meter radius area is considered as 100% fatality in 1 min.
In the 14.4 meter radius first degree burn in 10 sec.
In the 25.4 meter radius area will give pain after 20 seconds. Blistering unlikely.
Jet Fire
Red – 37.5 KW/m2
Yellow – 12.5 KW/m2
Green – 4 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 615
Over pressure / explosion for rupture of 1.0 cm copper pipe line of Hydrogen cylinder to PRV station
Results indicate:
In put Data Results of Computations
Stored quantity Cylinder bank
Visible Flash Fire Height 0.52 m
Mass of Gas 1 kgs Visible Flash Fire Width 0.26 m
Heat of combustion 42267 KJ/Kg Duration of Flash-Fire in Sec. 2 sec
Fuel-Air volume ratio in Flash
fire cloud
0.600 Radius of fuel-air cloud mixture 4.19 m
Stochiometric Fuel-Air Mixture 00:29 Total energy release 283720 KJ
Wind speed 2.05 m/s Max. Heat Radiation from 1 m from Flash Fire 750 KW/ m2
Gas Density 0.067 kg/m3 Combustion efficiency 0.5
Incident Intensity of Heat
Radiation ( IHR) at ground
level KW /m 2
IHR- Isopleth
Distance
( Meters )
Effect if IHR at Height of Simulation
37.5 19 Damage to process equipment. 100 % Fatal in 1 Min. 1 % fatal in 10
sec.
12.5 32 Min. to ignite wood (with flame contact). 1 % fatal in 1 min. 1st
deg.
burn in 10 sec.
4.0 57 Pain after 20 secs. Blistering unlikely.
Results
In the 19 meter radius area is considered as 100% fatality in 1 min.
In the 32 meter radius first degree burn in 10 sec.
In the 57 meter radius area will give pain after 20 seconds. Blistering unlikely.
Red – 37.5 KW/m2
Yellow – 12.5 KW/m2
Green – 4 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 616
Scenario: 3 – Release of Xylene
Results indicate:
Input Data
Stored quantity 15 MT
Wind speed 2.05 m/s
Consequence Results
Radiation Effects
Radiation
Level
(KW/m2)
Distance (meter)
(Category 1.5/F)
Effect if IHR at Height of simulation
4 31.68 This level is sufficient to cause personnel if unable to reach cover within
20s; however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 23.75 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 13.76 This level of radiation is assumed to give 100% fatality as outlined above.
Vapor Cloud Explosion
Radial
Distance (m)
Over Pressure
(psi)
Fatality lung
Rupture (%)
Eardrum
Rupture (%)
Structure
Damage (%)
Glass Rupture (%)
1.22 40.5 100.0 100.0 100.0 100.0
2.13 10.6 0.1 85.1 100.0 100.0
7.62 1.8 0.0 2.5 10.6 100.0
In case of Unconfined Vapor Cloud Explosion up to 1.22 meter is considered as 100% fatality and 100% ear drum
rupture radius.
In case of Unconfined Vapor Cloud Explosion up to 2.13 meter is considered as 100% structure damage and up to
7.62 meter 100% glass rupture area.
Flash Fire
Radiation
Level
(KW/m2)
Distance (meter)
(Category 1.5/F)
Effect if IHR at Height of simulation
4 40 This level is sufficient to cause personnel if unable to reach cover within 20s;
however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 24 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 9 This level of radiation is assumed to give 100% fatality as outlined above.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 617
Pool Fire Scenario: Flash Fire Scenario:
Red – 37.5 KW/m
2
Yellow – 12.5 KW/m2
Green – 4 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 618
Scenario – 4 Release of Toluene
This scenario considers release of Toluene from Storage Tank:
Results indicate:
Catastrophic Rupture
Input Data
Stored quantity - 17 KL
Wind speed - 2.05 m/s
Results indicate
Pool Fire Scenario
Radiation Level
(KW/m2)
Distance in meter Effect if IHR at Height of simulation
4 12.0 This level is sufficient to cause personnel if unable to
reach cover within 20s; however blistering of the skin
(second degree burn) is likely; 0: lethality
12.5 6.0 This level will cause extreme pain within 20 seconds and movement to
a safer place is instinctive. This level indicates around 6% fatality for
20 seconds exposure.
37.5 2.5 This level of radiation is assumed to give 100% fatality as outlined
above.
Vapor Cloud Explosion
Radial
Distance (m)
Over Pressure
(psi)
Fatality lung
Rupture (%)
Eardrum
Rupture (%)
Structure
Damage (%)
Glass Rupture
(%)
4.7 36.2 100.0 100.0 100.0 100.0
5.1 8.9 0.0 77.0 100.0 100.0
8.7 2.0 0.0 3.1 14.5 100.0
Fireball Scenario
Fireball Radius: 8.13656 m
Radiation Level
(KW/m2)
Distance in meter Injury Type
37.50 6.5 100% Fatal
12.5 11.5 1st
Degree burn
4 18.5 Pain after 20secs.
Flash Fire
Radiation Level
(KW/m2)
Distance in meter Injury Type
37.5 7.0 100% Fatal
12.5 12.0 Pain after 20secs.
4 20.0 Pain after 20secs.
SAFETY PRECUASION:
- Flame proof pumping and other equipments will be provided.
- Transfer will be done in close process,
- Double Static earthling and Jumper clips will be provided on flanges,
- Hydrant system and Fire extinguishers will be provided.
- Automatic Sprinklers will be provided.
- Tanker unloading procedure will be made and followed.
- Dyke around the tank will be provided.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 619
Pool Fire Fire Ball
Flash Fire
Green – 4 KW/m
2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 620
Scenario – 5 Release of Methanol
Results indicate:
Catastrophic Rupture
Input Data
Stored quantity - 25 KL
Wind speed – 2.05 m/s
Results indicate
Pool Fire Scenario
Radiation Level
(KW/m2)
Distance in meter
Effect if IHR at Height of simulation
4 24.0 This level is sufficient to cause personnel if unable to reach cover within
20s; however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 18.0 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 10.0 This level of radiation is assumed to give 100% fatality as outlined above.
Vapor Cloud Explosion
Radial Distance
(m)
Over Pressure
(psi)
Fatality lung
Rupture (%)
Eardrum
Rupture (%)
Structure
Damage (%)
Glass Rupture (%)
6.62 35.1 100.0 100.0 100.0 100.0
6.90 9.7 0.1 81.3 100.0 100.0
10.21 1.8 0.0 2.7 11.9 100.0
In case of Unconfined Vapor Cloud Explosion up to 6.62 meter is considered as 100% fatality and 100% ear drum
rupture radius.
In case of Unconfined Vapor Cloud Explosion up to 6.90 meter is considered as 100% structure damage and up to 10.21
meter 100% glass rupture area.
Results
37.5 KW/m2 IHR - In the 10.0 meter radius area is considered as 100% fatality in 1 min.
12.5 KW/m2 IHR - In the 18.0 meter radius first degree burn in 10 sec.
4 KW/m2 IHR - In the 24.0 meter radius area will give pain after 20 seconds. Blistering unlikely.
Fireball Scenario
Fireball Radius: 6.36 m
Fireball intensity of Heat Radiation (KW/m2) – 137.107
Fireball rate of Energy release (KJ/Sec)-69882.2
Fireball total energy released (KJ)- 98997.5
Fireball duration (Sec) – 1.40
Radiation Level
(KW/m2)
Distance in meter Injury Type
37.50 8 100% Fatal
12.5 14 1st
degree Burn
4 20 Pain after 20secs.
1.6 34 No Injury
Results
37.5 KW/m2 IHR - In the 8.0 meter radius area is considered as 100% fatality in 1 min.
12.5 KW/m2 IHR - In the 14.0 meter radius first degree burn in 10 sec.
4 KW/m2 IHR - In the 20.0 meter radius area will give pain after 20 seconds. Blistering unlikely.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 621
Pool Fire Flash Fire
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 622
Scenario – 6: Release of Ethanol
This scenario considers release of Ethanol from Storage Tank:
Input Data:
Storage capacity: 25 KL
Wind speed - 2.05 m/s
Results indicate:
Dispersion modeled as passive plume/cloud at distance 37.93 m and time 63.36 s
Pool radius 16.73 m
Cloud center has reached the UFL concentration 0.19 fraction at distance 5.171 m and time 5.943 s
Cloud center has reached the LFL concentration 0.043 fraction at distance 5.728 m and time 6.363 s
Cloud center has touched down at distance 5.393 m and time 6.155 s
Pool Diameter 33.70 m
Flame Length 21.47 m
Burn Rate 21.01 kg/s
Maximum Pool Radius 16.85 m
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 623
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 624
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 625
Scenario – 7 Release of HCl This scenario considers release of HCl from Storage Tank:
Results indicate:
Spill Pool evaporation modules for HCl Storage Tank catastrophic failure Input Data
Stored quantity - 10 KL
Wind speed - 2.05 m/s
Results indicate
LC50 – 149 ppm 44.69 meter
IDLH – 5 ppm 1532.66 meter
TLV –0.75 ppm 2943.00 meter
Results
LC50 HUMAN (149 ppm) area up to 44.69 meter, Immediate danger to life and health (5 ppm )
concentration area up to 1532.66 meter and TWA (0.75 ppm ) area up to 2943 meter. Therefore 1532.66
meter area in wind direction is considered as evacuation area.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 626
Measures to control and mitigate Emergency:
Measures to be taken to prevent such accident:
Priority will be given to Tanker to immediately enter the storage premises at site and will not be kept
waiting near the gate or the main road.
Security person will check License, TREM CARD, Fire extinguisher condition, required PPEs as per SOP laid
down.
Store officer will take sample as per sampling SOP from sampling point.
After approval of QC department unloading procedure will be allowed be started.
Following precautions will be adopted during unloading
Wheel stopper will be provided to TL at unloading platform.
Tanker unloading procedure will be followed according to check list and implemented.
Flexible hose connection will be done at TL outlet line and checked for no leakage.
Every time gasket will be changed.
The quantity remaining in the hose pipeline will be drained to a small container, which will be subsequently
transferred to the main storage tank thus ensuring complete closed conditions for transfer from road
tanker.
All TL valves will be closed.
Following precautions will be adopted Storage of such chemicals
Storage tank will be stored away from the process plant.
Tanker unloading procedure will be prepared and implemented.
Caution note and emergency handling procedure will be displayed at unloading area and trained all
operators.
NFPA label will be provided.
Required PPEs like full body protection PVC apron, Hand gloves, gumboot, Respiratory mask etc. will be
provided to operator.
Neutralizing agent will be kept ready for tackle any emergency spillage.
Safety shower, eye wash with quenching unit will be provided in acid storage area.
Material will be handled in close condition in pipe line.
Dyke wall will be provided to all storage tanks, collection pit with valve provision.
Double drain valve will provided.
Level gauge will be provided on all storage tanks.
Safety permit for loading unloading of hazardous material will be prepared and implemented.
TREM CARD will be provided to all transporters and will be trained for transportation Emergency of
Hazardous chemicals.
Fire hydrant system with jockey pump as per TAC norms will be installed.
Mitigation measures to control Emergency:
Safety Shower and eye wash will be provided away from the tank and unloading station.
Sand bags/ buckets will be provided near tank area.
Neutralizing medium (Lime and dry sand) will be kept ready near tank farm.
Emergency siren and wind sock will be provided.
Tele Communication system and mobile phone will be used in case of emergency situations for
communication.
First Aid Boxes and Occupational health centre will be made at site.
Emergency organization and team will be prepared.
Full body protection suite and other PPEs will be kept ready in ECC at site.
Emergency team will be prepared and trained for scenario base emergency. Like Toxic control team, Fire
control team, First aid team, communication and general administration team, Medical team etc.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 627
EMERGENCY RESPONSE
SPILL OR LEAK
· Do not touch damaged containers or spilled material unless wearing appropriate protective clothing.
· Stop leak if you can do it without risk.
· Use water spray to reduce vapors; do not put water directly on leak, spill area or inside container.
· Keep combustibles (wood, paper, oil, etc.) away from spilled material.
Small Spill
· Cover with DRY earth, DRY sand or other non-combustible material followed with plastic sheet to minimize
spreading or contact with rain.
· Use clean non-sparking tools to collect material and place it into loosely covered plastic containers for later
disposal.
· Prevent entry into waterways, sewers, basements or confined areas.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 628
Scenario - 8 Release of IPA
This scenario considers release of IPA from Storage Tank:
Results indicate:
Catastrophic Rupture
Input Data
Stored quantity - 12 KL
Wind speed – 2.05 m/s
Results indicate
Pool Fire Scenario
Radiation
Level (KW/m2)
Distance in meter
Effect if IHR at Height of simulation
4 62.0 This level is sufficient to cause personnel if unable to reach cover within 20s;
however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 40.0 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 22.5 This level of radiation is assumed to give 100% fatality as outlined above.
Vapor Cloud Explosion
Radial
Distance (m)
Over Pressure
(psi)
Fatality lung
Rupture (%)
Eardrum
Rupture (%)
Structure
Damage (%)
Glass Rupture (%)
6.50 36.7 100.0 100.0 100.0 100.0
6.83 8.4 0.0 73.3 100.0 100.0
10.02 1.9 0.0 2.8 12.8 100.0
In case of Unconfined Vapor Cloud Explosion up to 6.50 meter is considered as 100% fatality and 100% ear drum
rupture radius.
In case of Unconfined Vapor Cloud Explosion up to 6.83 meter is considered as 100% structure damage and up to
10.02 meter 100% glass rupture area.
Results
37.5 KW/m2 IHR - In the 22.5 meter radius area is considered as 100% fatality in 1 min.
12.5 KW/m2 IHR -In the 40.0 meter radius first degree burn in 10 sec.
4 KW/m2 IHR -In the 62.0 meter radius area will give pain after 20 seconds. Blistering unlikely.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 629
Fireball Scenario
Fireball Radius: 6.36m
Fireball intensity of Heat Radiation (KW/m2) – 134.186
Fireball rate of Energy release (KJ/Sec)- 68393.6
Fireball total energy released (KJ)- 96888.6
Fireball duration (Sec) – 1.40
Radiation Level
(KW/m2)
Distance in meter Injury Type
100.20 7.0 100% Fatal
37.5 11.0 100% Fatal
12.5 19.0 1st
degree Burn
9.96 23.0 Pain after 20secs.
4.0 35.0 Pain after 20secs.
1.54 59.0 No Injury
Results
37.5 KW/m2 IHR - In the 12.0 meter radius area is considered as 100% fatality in 1 min.
12.5 KW/m2 IHR - In the 19.0 meter radius first degree burn in 10 sec.
4 KW/m2 IHR - In the 35.0 meter radius area will give pain after 20 seconds. Blistering unlikely.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 630
Cloud Footprint
Maximum Concentration
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 631
Pool Fire Fire Ball
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 632
Scenario – 9 Release of Phenol This scenario considers release of Phenol from Storage Tank:
Results indicate:
Scenario : POOL FIRE
In put Data Results of Computations
Stored quantity 25 KL Max. IHR at flame centre height 63 Kw/m2
Pool diameter 10 (m) Flame centre height 15.6 meter
Pool liquid depth 2.8 (m) Maximum Flame width 14.6 meter
Wind speed 2.05 m/s Mass burning rate liquid 7.9 kg/ m2/min.
Liquid Density 1006 kg/m3 Flame burnout time 120 Mims.
Incident Intensity of Heat
Radiation ( IHR) at
ground level KW /m 2
IHR- Isopleth
Distance
( Meters )
Effect if IHR at Height of Simulation
37.5 5.45 Damage to process equipment. 100 % Fatal in 1 Min. 1 % fatal in 10
sec.
12.5 9.4 Min. to ignite wood (with flame contact). 1 % fatal in 1 min. 1 st deg.
burn in 10 sec.
4.0 16.6 Pain after 20 secs. Blistering unlikely.
Results
In the 5.45 meter radius area is considered as 100% fatality in 1 min.
In the 9.4 meter radius first degree burn in 10 sec.
In the 16.6 meter radius area will give pain after 20 seconds. Blistering unlikely.
Pool Fire
Green – 4 KW/m
2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 633
Scenario 10: Release of Nitric Acid
Catastrophic Rupture
Input Data
Stored quantity – 15 KL
Wind speed - 2.05 m/s
Vapor Density (Air=1) – 2.5
Results indicate
TLV – 4 ppm
Cloud Footprint:
Maximum Concentration:
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 634
Safety measures:
In case of contact with eyes, immediately flush eyes with plenty of water for at least 15 minutes. Cold
water may be used. Get medical attention immediately.
In case of contact with skin, immediately flush skin with plenty of water for at least 15 minutes while
removing contaminated clothing and shoes. Cover the irritated skin with an emollient. Cold water
may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical
attention immediately.
Wash with a disinfectant soap and cover the contaminated skin with an anti-bacterial cream. Get
medical attention.
If inhaled, remove to fresh air. If not breathing, give artificial respiration. If breathing is difficult, give
oxygen. Get medical attention immediately.
Evacuate the victim to a safe area as soon as possible.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 635
Scenario – 11: Release of Liq. Ammonia
Basis: Catastrophic Rupture unloading arm (4”) of road tanker and Resultant Pool Fire due to static charge.
Basic Input Data
Stored quantity 15 KL
Wind speed 1.62 m/s
Consequence Results
Radiation
Level
(KW/m2)
Distance (meter)
(Category 1.5/F)
Effect if IHR at Height of simulation
4 16.062 This level is sufficient to cause personnel if unable to reach cover within
20s; however blistering of the skin (second degree burn) is likely;
0: lethality
12.5 NR This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 NR This level of radiation is assumed to give 100% fatality as outlined above.
Fireball Radius 8.70 m
Cloud Footprint
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 636
Maximum Concentration
Pool Fire
Green – 4 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 637
Scenario – 12: Release of MDC MDC Tank Catastrophic Failure
Input Data
Stored quantity - 20 KL
Wind speed - 2.05 m/s
Results indicate
Pool Vapor Flow Rate – 26.8 kg/s
Pool Diameter – 72.76m
Cloud edge has reached the UFL concentration 0.191 fraction at distance 4.794 m and time 13.28s
Cloud edge has reached the LFL concentration 0.159 fraction at distance 10.1 m and time 20.86s
Cloud center has touched down at distance 0.1397 m and time 1.397s
Droplet totally evaporate at cloud centerline distance 0.2754 m
Dispersion modeled as passive plume/cloud at distance 167.5m and time 186.4s
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 638
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 639
Scenario – 13 Release of EDC
This scenario considers release of EDC from Storage Tank:
Results indicate:
Catastrophic Rupture
Input Data
Stored quantity - 20 KL
Wind speed - 2.05 m/s
Pool Fire Scenario
Radiation Level
(KW/m2)
Distance in
meter
Effect if IHR at Height of simulation
4 70.91 This level is sufficient to cause personnel if unable to reach
cover within 20s; however blistering of the skin (second
degree burn) is likely; 0: lethality
12.5 34.54 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 18.2 This level of radiation is assumed to give 100% fatality as outlined above.
Dispersion
Release Rate 1000 gms/sec. (assumption)
Hazard Level Concentration (ppm) Distance (meter)
LC50 1414.2 23.61
IDLH 300 48.93
TWA/ TLV 75 115
SAFETY PRECUASION:
- Flame proof pumping and other equipments will be provided.
- Transfer will be done in close process,
- Double Static earthling and Jumper clips will be provided on flanges,
- Hydrant system and Fire extinguishers will be provided.
- Automatic Sprinklers will be provided.
- Tanker unloading procedure will be made and followed..
- Dyke around the tank will be provided.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 640
DISPERSION ISOPLETH FOR EDC TANK CATASTROPHIC FAILURE
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 641
Pool Fire
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 642
Scenario-14 Release of Acetic Anhydride
Basic Input Data
Stored quantity 40 KL
Wind speed 2.05 m/s
Radiation Effects
Radiation Level
(KW/m2)
Distance (meter)
(Category 1.5/F)
Effect if IHR at Height of simulation
4 37.6 This level is sufficient to cause personnel if unable to reach cover within 20s;
however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 22.0 This level will cause extreme pain within 20 seconds and movement to a safer
place is instinctive. This level indicates around 6% fatality for 20 seconds
exposure.
37.5 NR This level of radiation is assumed to give 100% fatality as outlined above.
Results:-
Maximum Pool Radius is 21.8 m.
NR – Not Reached
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 643
Cloud Footprint
Maximum Concentration
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Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 644
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 645
Intensity Radiation for Pool Fire
Green – 4 KW/m2
Yellow – 12.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 646
Scenario – 15 Release of Sulfuric Acid
This scenario considers release of Sulfuric Acid from Storage Tank:
Results indicate:
Spill pool evaporation module for Sulphuric Acid due to Catastrophic Rupture of 40 KL Storage Tank
Input Data
Stored quantity - 20 KL
Wind speed – 2.05 m/s
Failure Mode: Catastrophic failure of 4” bottom nozzle and loss of containment
Density ( Air) – 1840 kg/m3
Release rate: 1000 g/s
Results indicate
LC50 – 510 mg/m3 38.26 meter
IDLH – 15 mg/m3 528.56 meter
TLV –1 mg/m3 792.29 meter
Results:-
LC50 HUMAN (510 mg/m3) area is up to 38.26 meter,
IDLH (15 mg/m3) concentration area is up to 528.56 meter and
TLV (1 mg/m3) area is up to 792.29 meter.
Therefore, 528.56 meter area in wind direction is considered as evacuation area.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 647
Scenario:
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 648
MITIGATION MEASURES FOR SULPHURIC ACID LEAKAGE:
Isolate the source if possible without risk.
If leakage is small, dilute with water and mop up, or absorb with an inert dry material and place in an
appropriate waste disposal container. If necessary: Neutralize the residue with a dilute solution of
sodium carbonate.
Absorb with DRY earth, sand or other non-combustible material.
Do not get water inside container. Do not touch spilled material. Use water spray curtain to divert
vapor drift.
Prevent entry into sewers, basements or confined areas.
Neutralize the residue with a dilute solution of sodium carbonate.
PREVENTIVE MEASURES TO AVOID SULPHURIC ACID LEAKAGE:
A dike will be provided to accommodate the full quantity in tank.
Periodic testing of storage tank will be done by competent person.
Provide exhaust ventilation or other engineering controls to keep the airborne concentrations of
vapors below their respective TLVs. Storage tank vent is connected to scrubber system.
Flange guard provided to prevent splash of material.
Level interlock
Keep container dry. Never add water to this product.
In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical
advice immediately and show the container or the label.
Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, organic
materials, metals, alkalis, moisture.
Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area.
While handling always use face shield. Full suit. Vapor respirator. Be sure to use an approved/certified
respirator or equivalent.
Ensure that eyewash stations and safety showers are proximal to the work-station location.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 649
Scenario – 16 Release of Bromine
This scenario considers release of Bromine from Storage Tank:
Results indicate:
Spill Pool Evaporation for Bromine 8 KL day tank catastrophic failure
Scenario : Puff release
Input Data Results of Computations
Stored quantity 12 MT
Evaporation rate 1500 g/s
End point
(meter)
LC50 Human 1075 ppm 50
IDLH value 3.0 ppm 1418
Results
LC50 HUMAN (1075 ppm) area up to 50 meter, IDLH (Immediate danger to life and health)
concentration (3.0 ppm) area up to 1418 meter and TWA (0.1 PPM) area.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 650
Catastrophic Rupture
Input Data
Stored quantity - 12 MT
Wind speed - 2.05 m/s
Results indicate (Puff Release)
LC50 – 1075 ppm 27.50
IDLH – 3 ppm 292.84
TLV – 0.1 ppm 787.33
Safety Precaution:
Preventive maintenance of FLT. Train and license driver will be employed to drive FLT.
Limit switch, interlock will be provided, Apron, Hand gloves, gumboot, helmet, goggles will be provided.
Apron, Hand gloves, gumboot, helmet, goggles will be provided.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 651
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 652
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 653
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 654
Measures to control and mitigate Emergency of Bromine:
Bromine emergencies:
Transportation Emergencies
Evacuate the area in down wind direction:
For Bromine evacuate area in down wind direction up to 0.6 km ( 600 meter) in small
Spillage and in case of large spillage, evacuate the area in down wind direction 3.1 kms (3100 meters).
In emergency situations resulting from vehicle accidents:
1. Notify the local police, fire departments, emergency responders and the carrier.
2. Isolate the area.
3. Any person not dressed in proper protective clothing and not using a NIOSH approved self-contained
breathing apparatus should be kept a safe distance away.
4. Call to the supplier.
5. Seek immediate medical assistance for those injured and follow recommended first aid procedures.
Leaking Containers
6. When handling a leaking bottle personal protective clothing, goggles and NIOSH approved self contained
breathing equipment must be worn.
7. Clear contaminated area of non-essential personnel and send them to assembly point.
8. Maintain a slight ammonia atmosphere throughout the clean up. Carefully release anhydrous ammonia gas
to neutralize bromine vapor. The ammonia gas will convert bromine to white ammonium bromide “smoke.”
9. Do not allow liquid bromine and liquid ammonia to combine; a violent reaction will occur. Ammonia (16 to
25% by volume) can form an explosive mixture with air.
10. Pour hypo solution*, lime and water slurry or soda ash solution over the spill. Hypo-bromine reactions
produce hydrobromic acid.
11. Dry sodium thiosulfate and liquid bromine produce a violent reaction; do not mix them.
12. Using cold water, wash neutralized bromine into a sump for transfer to an approved waste disposal facility
where the waste can be processed.
13. Ventilate the area to remove the ammonium bromide and any bromine fumes. Scrub the floors and
equipment with soap and water.
First Aid Procedure
14. Immediate medical assistance is required if bromine is swallowed, inhaled or has contacted the eyes or
skin.
15. If bromine has been ingested, do not give anything by mouth. Seek medical attention immediately. Do not
induce vomiting.
16. If bromine has been inhaled, move the exposed person to a well ventilated area. Seek medical attention
immediately. The victim should be placed in a comfortable sitting or partly reclining position. The exposed
individual should avoid exertion. If vomiting occurs, turn the patient on his side to avoid choking. Keep the
patient warm. If the patient is coughing and showing signs of respiratory distress, properly trained personnel
should administer oxygen.
17. For skin contact, the affected area must be flooded immediately with large amounts of clean water from a
safety shower or other appropriate source of flowing water. Seek medical attention immediately. All
contaminated clothing, including shoes, should be removed as quickly as possible while the victim is under the
shower. Washing should be continued for a minimum of 30 minutes. If possible, continue to wash the affected
area during transport to medical facilities. (Extended wash times of two hours or more have proven beneficial.)
18. If bromine liquid or vapor contacts the eyes, they must be irrigated immediately with large amounts of
running water. Eye wash stations are preferable for irrigation. If one is not available, a hose, water source with
a liberal, gentle flow may be utilized. The eyelids must be held apart during irrigation to ensure contact of
water with all accessible tissues of the eyes and lids. Eyes should be washed continuously for a minimum of 30
minutes. If possible, continue flushing the eyes while transporting the employee to a physician. In all cases of
bromine injury, obtain immediate medical attention. Provide emergency personnel with information about all
materials used by the person and provide appropriate information about bromine and first aid procedures.
EMERGENCY RESPONSE
ELIMINATE all ignition sources (no smoking, flares, sparks or flames in immediate area).
· Do not touch damaged containers or spilled material unless wearing appropriate protective clothing.
· Stop leak if you can do it without risk.
· Prevent entry into waterways, sewers, basements or confined areas.
· Absorb or cover with dry earth, sand or other non-combustible material and transfer to containers.
· Do not get water inside containers.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 655
Scenario - 17: Release of Ethyl Acetate
Basis: Catastrophic Rupture unloading arm (4”) of road tanker and Resultant Pool Fire due to static charge.
Basic Input Data
Stored quantity 20 KL
Wind speed 2.05 m/s
Consequence Results
Radiation
Level
(KW/m2)
Distance (meter)
(Category 1.5/F)
Effect if IHR at Height of simulation
4 106.68 This level is sufficient to cause personnel if unable to reach cover within
20s; however blistering of the skin (second degree burn) is likely;
0: lethality
12.5 66.16 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 39.33 This level of radiation is assumed to give 100% fatality as outlined above.
Max. Pool Radius 18.32
Cloud Footprint
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 656
Maximum Concentration
Pool Fire
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 657
Scenario – 18 Release of Hexane
This scenario considers release of Hexane from Storage Tank:
Results indicate:
Catastrophic Rupture
Input Data
Stored quantity - 4 KL
Wind speed – 2.05 m/s
Density ( Air) – 869 kg/m3
Pool Fire Scenario
Radiation Level
(KW/m2)
Distance in meter
Effect if IHR at Height of simulation
4 16.4 This level is sufficient to cause personnel if unable to reach cover within 20s;
however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 11.8 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 7.6 This level of radiation is assumed to give 100% fatality as outlined above.
Pool diameter – 2.35 m
Maximum Flame width – 4.12 m
Results
37.5 KW/m2 IHR - In the 7.6 meter radius area is considered as 100% fatality in 1 min.
12.5 KW/m2 IHR - In the 11.8 meter radius first degree burn in 10 sec.
4 KW/m2 IHR - In the 16.4 meter radius area will give pain after 20 seconds. Blistering unlikely.
Pool Fire
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 658
Scenario 19: Release of Tetrahydrofuran
Results indicate:
Input Data
Stored quantity - 4 KL
Wind speed – 2.05 m/s
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 659
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 660
Scenario – 20 Release of Carbon Disulphide
This scenario considers release of CS2 from Storage Tank:
Results indicate:
Catastrophic Rupture
Input Data
Stored quantity - 150 KL
Wind speed – 2.05 m/s
Pool Fire Scenario
Radiation Level
(KW/m2)
Distance in meter
Effect if IHR at Height of simulation
4 240.5 This level is sufficient to cause personnel if unable to reach cover within 20s;
however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 118.4 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 55.2 This level of radiation is assumed to give 100% fatality as outlined above.
Maximum Pool Radius – 45.68 m
Results
37.5 KW/m2 IHR - In the 55.2 meter radius area is considered as 100% fatality in 1 min.
12.5 KW/m2 IHR - In the 118.4 meter radius first degree burn in 10 sec.
4 KW/m2 IHR - In the 240.5 meter radius area will give pain after 20 seconds. Blistering unlikely.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 661
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 662
Pool Fire
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 663
Scenario – 21 Release of Ethylene Diamine
This scenario considers release of EDA from Storage Tank:
Results indicate:
Catastrophic Rupture
Input Data
Stored quantity - 250 KL
Wind speed – 2.05 m/s
Pool Fire Scenario
Radiation Level
(KW/m2)
Distance in meter
Effect if IHR at Height of simulation
4 283.95 This level is sufficient to cause personnel if unable to reach cover within 20s;
however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 194.25 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 83.69 This level of radiation is assumed to give 100% fatality as outlined above.
Maximum Pool Radius – 61.93 m
Results
37.5 KW/m2 IHR - In the 83.69 meter radius area is considered as 100% fatality in 1 min.
12.5 KW/m2 IHR - In the 194.25 meter radius first degree burn in 10 sec.
4 KW/m2 IHR - In the 283.95 meter radius area will give pain after 20 seconds. Blistering unlikely.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 664
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 665
Pool Fire
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 666
Scenario – 22 Release of Phosphorus Trichloride
This scenario considers release of PCl3 from Storage Tank:
Catastrophic Rupture
Input Data
Stored quantity - 150 KL
Wind speed – 2.05 m/s
Results indicate:
Maximum Pool Radius – 61.93 m
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 667
Scenario - 24 Unconfined Pool Fire Simulations for Drum Storage Area
Catastrophic Rupture
Input Data
Stored quantity - 200 Lit (200 lit X 100 drums)
Wind speed – 2.05 m/s
Results indicate
Pool Fire Scenario
Radiation Level
(KW/m2)
Distance in meter
Effect if IHR at Height of simulation
4 50.5 This level is sufficient to cause personnel if unable to reach cover within 20s;
however blistering of the skin (second degree burn) is likely; 0: lethality
12.5 37.6 This level will cause extreme pain within 20 seconds and movement to a
safer place is instinctive. This level indicates around 6% fatality for 20
seconds exposure.
37.5 19.80 This level of radiation is assumed to give 100% fatality as outlined above.
Fire Ball Scenario
Radiation Level
(KW/m2)
Distance in meter Injury Type
4 65.0 Pain after 20secs.
12.5 42.5 1st
degree Burn
37.50 25.0 100% Fatal
MITIGATION MEASURES:
Isolate the source if possible without risk.
If leakage is small, dilute with water and mop up, or absorb with an inert dry material and place in an
appropriate waste disposal container. If necessary: Neutralize the residue with a dilute solution of
sodium carbonate.
Absorb with DRY earth, sand or other non-combustible material.
Do not get water inside container. Do not touch spilled material. Use water spray curtain to divert
vapor drift.
Use water spray to reduce vapors.
Prevent entry into sewers, basements or confined areas.
Neutralize the residue with a dilute solution of sodium carbonate.
Trained man power for fire fighting /toxic resale
PREVENTIVE MEASURES:
A dyke will be provided to accommodate the full quantity stored in all the drums.
Drums will be stored in designated area.
Provide exhaust ventilation or other engineering controls to keep the airborne concentrations of
vapors below their respective TLVs.
Never add water to this product.
In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical
advice immediately and show the container or the label.
Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, organic
materials, metals, alkalis, moisture.
Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area.
While handling always use face shield. Full suit. Vapor respirator. Be sure to use an approved/certified
respirator or equivalent.
Ensure that eyewash stations and safety showers are proximal to the work-station location.
Mock drills –Regularly
Display of Hazards & how to controll
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 668
Pool Fire Fire Ball
Green – 4 KW/m2
Yellow – 12.5 KW/m2
Red – 37.5 KW/m2
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 669
6.1.6 RISK ASSESSMENT SUMMARY
From the Risk Assessment studies conducted, it would be observed that by and
large, the risks are confined within the factory boundary walls.
Based on these studies company has been proposed to plan its facility sitting as well
as location of operator cabin, open area, etc.
Company has to increase awareness programme in the surrounding vicinity and
educate people for safe evacuation at the time of toxic release.
A HAZOP study to be carried out for all product plant and storage facilities.
Induction safety course to be prepared and trained all new employees before
starting duties in plant.
Ensure periodically process safety knowledge & equipment safety provision
6.1.6.1 PROCESS SAFETY
Safety measures to be adopted from the design stage.
Safety Valve and pressure gauge are to be provided on reactor and its jacket (if jacket is
provided).
Utility like Chilling, cooling, vacuum, steaming and its alternative are to be provided to
control reaction parameters in a safe manner.
Free Fall of any flammable material in the vessel is to be avoided.
Static earthing provision is to be made at design stage to all solvent handling
equipments, reactors, vessels & powder handling equipments.
Any reaction upsets will be confined to the reaction vessel itself.
All emergency valves and switches and emergency handling facilities are to be easily
assessable.
Further all the vessels are to be examined & will be examined periodically by a
recognized competent person under the Gujarat Factory Rules.
All the vessels and equipments are to be earthed appropriately and protected against
Static Electricity. Also for draining in drums proper earthing facilities is to be provided.
Exothermic/Run away reaction- to be provide Knock out tank & double safety &
interlocks
Materials shall be transferred by pumping through pipeline or by vacuum from drums.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 670
All solvents and flammable material storage tanks shall be stored away from the
process plant and required quantity of material is to be charged in reactor by pump.
Jumpers are to be provided on all solvent handling pipeline flanges.
Caution note, safety posters, stickers, periodic training & Updation in safety and
emergency preparedness plan shall be displayed and conducted.
Flame proof light fittings will be installed in the plant.
All the Plant Personnel shall be provided with Personal Protection
Equipments to protect against any adverse health effect during operations, leakage,
spillages or splash. PPE like Helmets, Safety Shoes, Safety Glasses, Acid-Alkali Proof
Gloves etc. are to be provided to the employees.
All employees shall be given and updated in Safety aspects through periodic training in
safety.
Material Safety Data Sheets of Raw Materials & Products will be readily available that
the shop floor.
6.1.6.2 FOR HAZARDOUS STORAGE TANK FARM
Tank farm shall be constructed as per explosive department requirement and separation
distance will be maintained.
Tanks shall be located and marked in designated area of hazardous chemical storage.
Static earthing provision shall be made for road tanker as well as storage tank.
Tanks of proper MOC shall be selected.
Flame arrestor with breather valve shall be provided on vent line.
Road tanker unloading procedure /Check list to be implemented.
Fire load calculation shall be done and as per fire load Hydrant System will be provided
as per NFPA std. and Fire extinguishers shall be provided as per fire load calculation.
Spark arrestor shall be provided to all vehicles in side premises.
Flame proof type equipments and lighting shall be provided.
Lightening arrestor shall be provided on the top of chimney.
Trained and experience operator shall be employed for tank farm area.
NFPA label (hazard identification) capacity and content shall be displayed on storage
tank.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 671
Solvents shall be transferred by pump only in plant area and day tank shall be provided.
Overflow line returns to the storage tank or Pump On-Off switch shall be provided near
day tank in plant.
Jumpers shall be provided on solvent handling pipe line flanges.
Flexible SS hose shall be used for road tanker unloading purpose and other temperature
connection.
All tanks shall be uniformly tagged.
Level indicator shall be provided in tanks.
Dyke shall be provided.
Industrial type electric fittings shall be provided.
Adequate fire fighting equipments shall be provided.
Anti corrosive paint shall be done.
Safety instruction board shall be displayed.
6.1.6.2 FOR DRUM/CARBOY STORAGE AREA
Some chemicals shall be received at plant in drums/Carboys by road truck and stored in a
drum/Carboy storage area.
FLP type light fittings shall be provided.
Proper ventilation shall be provided in godown.
Proper label and identification board /stickers shall be provided in the storage area.
Conductive drum pallets shall be provided.
Drum handling trolley /stackers/fork lift shall be used for drum handling.
Separate dispensing room with local exhaust and static earthing provision shall be made.
Materials shall be stored as per its compatibility study and separate area will be made for
flammable, corrosive and toxic chemical drums storage.
Smoking and other spark, flame generating item shall be banned from the Gate.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 672
6.1.6.3 TRANSPORTATION
Road tanker unloading procedure shall be in place and is implemented for safe
unloading of road tanker.
Static earthing provision shall be made for tanker unloading.
Earthed Flexible Steel hose shall be used for solvent unloading from the road tanker.
Fixed pipelines with pumps shall be provided for solvent transfer up to Day
tanks/reactors.
Double mechanical seal type pumps shall be installed.
NRV provision shall be made on all pump discharge line.
Dry run /High temperature protection to be provided.
6.1.7 OTHER RISK REDUCTION OPPORTUNITIES
The following opportunities are to be considered as a potential means of reducing identified
risks during the detailed design phase:
Buildings and plants structures shall be designed for cyclone floods and seismic
events to prevent structural collapse and integrity of weather (water) proofing for
storage of goods;
Provision for adequate water capacity to supply fire protection systems and critical
process water;
Isolate people from load carrying/mechanical handling systems, vehicle traffic and
storage and stacks locations;
6.1.8 RECOMMENDATIONS FOR ALARP
The following actions shall be particularly recommended to be implemented in order to
ensure ALARP (As Low As reasonably practical) performance in the operation: Maintain and
ensure effectiveness of all the safety measures, among others through the following actions:
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 673
Raw Material Storage Area
- The raw material storage area should be declared as a prohibited area and should be
provided having at least two exits, “No Smoking” and “Prohibited Area” display
boards, as applicable should be provided at site.
- Regular inspection of tanks/drums/carboys containing raw material to be done to
take care.
- Periodic site inspection should be carried out to ensure that there is no leakage from
any of the drums in the ware house.
- Fire hydrant system needs to be provided in storage area as per TAC standards.
- Smoke detector and fire alarm systems need to be provided.
- Provision of fire doors in ware house area.
Fire access for Tank Farm area and Ware Houses
- Fire access roads should be provided to storage area. The storage tanks/area should
have suitable fire protection and fire fighting facility.
The following features are also important for the project by taking the layout into
consideration:-
Hinged doors swing outward in an explosion.
Window panes (if installed) shall be shatterproof or plastic in frame.
Floors, walls and ceilings are to be designed and installed to limit the generation and
accumulation of static electricity.
All doors must be fire resistant. Floors, walls and ceilings shall be designed for at
least 2 h of fire resistance.
Walls or partitions shall be continuous from floor to ceiling, and securely anchored.
Integrity of the wall should be ensured i.e. blast wall not to be broken or drilled as
that can leads to weak spots.
The building shall be constructed of non-combustible materials, on a substantial
frame.
Restrained deflagration vent panels shall be present.
There shall be adequate ventilation, and any heating in rooms is limited to steam,
hot water, or other indirect means.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 674
Electrical Safety for Whole Facility
Electrical Safety: All cables and electric fittings shall be constructed, installed,
protected, operated and maintained in such a manner so as to prevent risk of open
sparking.
6.1.9 FIRE FIGHTING SYSTEM
M/s. Greentec chemicals Pvt. Ltd., Management has taken into consideration fire
prevention measures at the project planning and during plant commissioning stage to avoid
any outbreak of fire. But looking to the hazardous nature of process and the chemicals that
are to be handled and processed, the chances of outbreak of fire cannot be totally ignored.
Hence to tackle such a situation a good well laid fire protection system will be provided in
the factory. Details of fire fighting are given in Table 6.5.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 675
TABLE 6.5
FACILITIES FOR FIRE FIGHTING
Fire Extinguisher Type Fire Fire Hydrant Valve Branch Mech Sprinkler Wind First
DCP (Kgs) Foam CO2 (Kgs) Sand
Safety
SCBA ELBA Hose FEH Single Foam system Sock Aid
Plant/Location
5 6 10 9ltr 2 4.5 22.5 Bucket Shower SET SET Reel Hydrant
Fire
Hose Short TP FB
5x
Water
cum
Foam
Monitor ltr Box
Fire Pump
House 1 1 2 4 1 2 1800
Fungicide Plan 1 1 6 4 20 4 1 10 1 10 2 500 4 2 2
Insecticide
plant 1 1 6 4 10 2 1 10 1 10 2 500 4
1 1
Intermediate
plant 1 1 6 4 12 2 1 10 1 10 2 500 4
1 1
Herbicide
plant 1 1 6 4 15 2 1 1 1 10 2 500 4
1 1
Solvent Yard 1 4 2 8 4 4 7 2 1 1 200
Tank farm 1 1 1 1 1 4 1 4 4 3 2 1 2 1 1
ETP 6 1 3 2 2 4 1
R&D 1 1 1 1 2 2 2 2 1
QC Lab 1 1 2 2 1 2 1 1 1 1 1
QC UPS Room 1 1
Utility 1 3 4 4 8 1 1
Finished
product
Area(WH)
3 2 2 4 2 1
1
Compressor
room 2 1 1 1 1
1
Panel
room(nr.toilet) 1 1 1 2 1
LFR 1
Canteen 2 1 2 1 1
ADM 1 1 2 1 2 1 1 1
Main Gate
(Security) 5 3 2 2 1 2 4
1 1
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 676
Fire Extinguisher Type Fire Fire Hydrant Valve Branch Mech Sprinkler Wind First
DCP (Kgs) Foam CO2 (Kgs) Sand
Safety
SCBA ELBA Hose FEH Single Foam system Sock Aid
Plant/Location
5 6 10 9ltr 2 4.5 22.5 Bucket Shower SET SET Reel Hydrant
Fire
Hose Short TP FB
5x
Water
cum
Foam
Monitor ltr Box
Ambulance 2 1
Store 8 3 4 4 2 4 1 1 2 4 1 1
OHC 1 2 1
Power House 1 1 3 1 2
R&M
Workshop 1
1
Explosive tank
fram 2 2 1 2 2 4 1 1 200 1
Fabrication
workshop 2 1
Stand by Fire
Pump House 1 1 1 2 2
19 20 15 19 9 45 13
54 4 67 12 33 4 23 3
Total 124 35 11 18 7 54 50 87 30 11 3200 20 9 18
Main and Alternative water storage cap. : 1000 KL
Single Hydrant Point (Jet Type) : 33 No.
Water Monitor fixed : 11 No.
Water Monitor Trolley Mounted : 02 No.
Water Monitor lifting height : Water/Foam throws 45 to 60 meters at an angle of 30’ in still air. Water/Foam flow
1750 to 2600 LPM.
No. of Fire Sand Storage : 35 No. Fire sand bucket
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 677
DETAILS OF FIRE HYDRANT PUMPS
SR.
NO.
NAME OF EQUIPMENT CAPACITY/
QUANTITY
DISCHARGE TAG.NO. LOCATION MAKE
1 Water Reserve Tank 1000 KL Fire Pump House FWS/01 Fire Pump house RCC
2 Jockey Pump 12.5 HP 10.8 m3/hr JP-01 Fire Pump house Kirloskar
3 Main Pump 75 HP 171 m3/hr MP-01 Fire Pump house Kirloskar
4 Diesel Pump 92 HP 171 m3/hr DP-01 Fire Pump house Kirloskar
5 D-watering pump 12.5 HP - DWP-01 Fire Pump house -
6 Diesel Tank 200 Liter - - Fire Pump House -
Other fire fighting facilities proposed to be installed at site:
Fire load calculation shall be carried out and Fire Extinguishers at different locations
shall be provided (as mentioned in above table) as per the TAC guidelines.
Working staff shall be given training to operate DCP and CO2 extinguishers.
Fire Hydrant Network shall be installed as per the calculated requirement for fire
fighting.
A main fire pump with a capacity of 50 m3/hr @ 10 Bar/cm2 is to be installed.
A stand-by diesel pump with equal capacity (50 M3/Hr @ 10 Bar/cm2) is to be
installed. This pump will be used for fire fighting in case of power failure.
A fire water reservoir with holding capacity of 300 m3 of water shall be provided.
First Aid Training will be imparted to employees by designated first aid trainers.
6.2 DISASTER MANAGEMENT PLAN
M/s. Greentec Chemicals Pvt. Ltd. shall develop the emergency management system to
tackle the emergency situation, apart from its emergency management system. The detail of
disaster management system is discussed in the following section.
6.2.1 DEFINING THE NATURE OF EMERGENCY
6.2.1.1 LEVEL OF EMERGENCY CAN BE CLASSIFIED IN THREE CATEGORIES.
LEVEL - 1:
The leakage or emergency, which is confinable within the plant, premises. It may be due to -
a) Small fire in the plant
b) Low toxic gas release for short duration.
c) Collapsing of equipment that do not affect out side premises.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
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LEVEL - 2:
The emergency, which is confinable within the factory premises. It may arise due to -
a) Major fire inside the factory premises.
b) Medium scale explosion confined to the factory premises.
c) Heavy toxic / flammable gas leakage for short duration.
LEVEL - 3:
The emergency, which is not confinable within the factory premises and general public in
the vicinity likely to be affected. It may arise due to -
a) Explosion of high magnitude affecting the adjacent area
b) Heavy / Profuse leakage of toxic / flammable gases for a long duration.
6.2.2 OBJECTIVES OF EMERGENCY MANAGEMENT SYSTEM
The objectives of the emergency management system are summarized as under.
To identify and assess types of emergencies due to different types of hazards.
To work out plan with all provisions to handle emergencies and safeguard employees
and people in the vicinity of the factory.
To provide for emergency preparedness and the periodical rehearsal of the plan.
To plan mode of proper communication and actions to be followed in the event of
emergency.
To keep all necessary information with respect to hazard/accident control and
emergency contacts in one document for easy and speedy reference.
To inform employees, general public and the authorities about the hazards/risk if any
and the role to be played by them in the event of emergency.
To control and contain the accident.
To effect rescue and treatment of casualties.
To inform and help relatives of casualties.
To secure rehabilitation of affected area and restore normalcy.
To provide information to media and government agencies.
To preserve record, equipment etc. for investigating cause of emergency.
To be ready for “mutual aid” if need arises to help neighboring units.
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6.2.3 STRUCTURE OF EMERGENCY MANAGEMENT SYSTEM
M/s. Greentec Chemicals Pvt. Ltd. shall develop an emergency management team. The
management structure includes the following personnel’s;
Incident Controllers and Deputy Incident Controllers
Site Main Controllers
Key Personnel’s
Essential Workers
Assembly points
Emergency control center
Fire control arrangements
Medical arrangements
Other arrangements
6.2.3.1 INCIDENT CONTROLLER AND DEPUTY INCIDENT CONTROLLER
His primary duty is to take charge at the scene of the incident. In the initial stages he may be
required to take decision involving the operation of the other plants or to stop or continue
any process and operation of the other plants or to stop or continue any process and to take
technical decision to control the incident. Therefore he should be fully knowledgeable for
this purpose. He is a factory Manager. Appointed such person for all shifts including
holidays. Any one incident controller must be available at any time. Fixed their duties that
way. The duty is appointed to take the charge of incident controller if he is not available due
to any reason. He is equally competent. The incident controllers have adequate means of
communicating with the emergency control center by telephone or runner.
His responsibilities/duties are as follows:
1. Immediately being aware of the emergency and its location, he will proceed to the
scene. On arrival he wills.
2. Assess the scale of emergency and decide if a major emergency exist or is likely. On
his decision, he will activate the on site plan and if necessary the off site emergency
plan.
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3. Assume the duties of the site Main Controller pending the latter’s arrival for this
purpose he will depute his Deputy Incident Controller on the scene and he will go to
the control center. Particularly he will:
3.1. Direct the spitting down and evacuation of plant and areas likely to be
affected the emergency.
3.2. Ensure that the outside emergency services, including mutual aid, have been
called in.
3.3. Ensure that key personnel have been called in.
4. Direct all operations with in the affected area with the following properties.
4.1. Secure the safety of personnel.
4.2. Minimize damage to plant, property and the environment.
4.3. Minimize loss of material.
5. Direct rescue and fire fighting operations until the arrival of the outside fire bridged,
when he will relinquish control to the head of the Fire Bridged.
6. Search for casualties.
7. Evacuate non-essential workers to the assembly points.
8. Set up a communications point and establish/telephone/messenger contact as
appropriates with the emergency control center.
9. Give advice and information as required to the head of the Fire Bridged and other
emergency services.
10. Brief the site main controller and keep informed of developments.
11. Preserve evidences that will be necessary for subsequent inquiry in to the cause of
the emergency and concluding preventive measures.
6.2.3.2 SITE MAIN CONTROLLER
He has overall responsibilities for directing operations and calling outside help form
Emergency Control center. As he is required to take decisions by collaboration between the
senior manager at the site (works) and the senior officers of the outside services, he is the
senior manager or top execute.
His responsibilities / duties are as follows:
Immediately being aware of the emergency, he will go to the Emergency Control Room. On
arrival he will-
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
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Relieve the Incident Controller of responsibility for overall main control.
On consultation with the Incident Controller decide whether major emergency exist
and on declaration of a major emergency, ensure that the outside emergency
services and mutual help are called, the off-site plan activated and if necessary,
nearby factories and population are informed.
Ensure that the key personnel are called in.
Exercise direct operational control of those parts of the works outside the affected
area.
Continually review and assess possible developments to determine the most
probable course of events.
Direst the safe close down and evacuation of plants in consultation with the Indirect
Controller and key personnel. If necessary, arrange for evacuation of neighboring
population.
Ensure that consulates are receiving adequate attention. Arrange for hospitalization
of victims and additional help if required. Ensure that the relatives are advised.
Inform and liaise with the Chief Officer of the Fire and Police Services, District
Emergency Authority and with the Factory Inspectorate and experts on health and
safety. Provide advice on possible effects on areas outside the factory.
In the case of prolonged emergencies involving risk to outside areas by wind blown
materials, contact the local meteorological office to receive early notification of
impending changes in weather conditions.
Ensure the accounting for personnel and rescue of missing persons.
Control traffic movement within the factory.
Arrange for a chronological record of the emergency to be maintained.
Where the emergency is prolonged, arrange for the relief of personnel and the
provision of catering facilities.
Issue authorized statements to the news media. Where necessary, inform Head
office.
Ensure that proper consideration is given to the preservation of evidence. Arrange
for photographs / video.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 682
Control rehabilitation of affected areas and victims on causation of the emergency.
Do not restart the plant unless. It is ensured safe to start and cleared by the
authorities.
6.2.3.3 KEY PERSONNELS
Other key personnel are required to provide to and implement the decisions made by the
Site Main Controller in the light of information received on the developing situation at the
emergency. Such key personnel will include the senior managers responsible for safety,
security, gas and spill control, pollution control, Communication system including telephone,
wireless, messengers etc, medical services, transport, engineering, production, technical
services (including utilities, laboratories) stores and personnel (including welfare, canteen,
shelters etc).
As necessary, they will decide the actions needed to shutdown plants, evacuate personnel,
carry out emergency engineering work, arrange for supplies of equipment, utilities ( fuel
water, power etc ) carry out atmospheric tests, provide catering facilities, liaise with police,
fire brigade, emergency planning authority, factory Inspectorate, hospitals, neighboring
industries and population, assembly points, outside shelters, mutual aid centers, relatives of
casualties, press and so on, under the direction of the Site Main Controller. At the
declaration of a major emergency, all key personnel and others called in to assist shall
report to the Emergency Control Center. They shall be available at any time on duty or on
call on off – duty or holiday.
6.2.3.4 ESSENTIAL WORKERS
A taskforce of essential trained workers (expert teams) will be available to get the work
done by the incident control and the site main controller. Such work will include:
Fire righting, gas leak and spill control till a fire Brigade takes the charge.
To help to the Fire brigade and mutual aid teams. It is so required.
Shutting down plant and making it safe.
Emergency engineering work e.g. Isolating equipment, materials, process, providing
temporary by-pass lines, safe transfer of material, urgent repairing or replacement,
electrical work etc.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
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Provision of emergency power, water, lighting, instruments, equipments, materials
etc.
Movement of equipment, special vehicle and transport to or from the scene of the
incident.
Search, evacuation, rescue and welfare.
First-aid and medical help.
Moving tankers or other vehicles from area of risk.
Carrying out atmospheric test and pollution control.
Assistance at casualty’s reception areas to record details of casualties.
Assistance at communication center to handle out going and incoming calls and to
act as messengers if necessary.
Manning of works entrances in liaison with the police to direct emergence vehicles
entering the work, to control traffic leaving the works and turn away or make
alternative safe arrangements for visitors, contractors and other traffic arriving at
the works.
Informing surrounding factories and the public risk directed by the Site Main
Controller.
Any special help required.
6.2.3.5 ASSEMABLY POINT
In affected and vulnerable plants, all non-essential workers (who are not assigned any
emergency duty) shall evacuate the area and report to a specified assembly point. Each
assembly point will be clearly marked by a conspicuous notice and provided with an
identification number e.g. ASSEMBLY POINT -1. Mark such points permanently for the notice
of people.
Each assembly point is sited in a safe place, well away from areas of risk and least affected
by the down wind direction. More than one assembly point is needed (1) to ensure that
employees do not have to approach the affected area to reach the point. (2) In case any
assembly point lies in the path of wind-blown harmful materials, e.g. toxic gas.
Each assembly point is manned by a nominated person(s) to record the names and
departments of those reporting there.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 684
SAFE ASSEMBLY POINTS
IDENTIFICATION
Sr.No. OF THE
ASSEMBLY
POINT
LOCATION ACCOMMODATION
CAPACITY
1 Nr HR /
ADMN
Garden
Approx 100 People
2 Near boiler
house
Gate 3
(emergency
gate)
Approx 100 People
6.2.3.6 EMERGENCY CONTROL CENTER
The Emergency Control Center (or Room) is the place from which the operations to handle
the emergency are directed and co-ordinate. It will be attended by the site Main Controller,
key personnel and senior officers of the Fire, police, factory Inspectorate, and district
authorities and emergency services. The Center is equipped to receive and transmit
information and directions from and to the incident controller and areas of the works as
well as outside. Have equipment for logging the development of the incident of the assist
the controllers to determine any necessary action. In addition to the means of
communication, the center is equipped with relevant data and equipment, which will assist
those meaning the center to be conversant with the developing situation and enable them
to plan accordingly. It is sited in an area of minimum risk and close to a road to allow for
ready access by a radio-equipped vehicle for use it other systems fails or extra
communication facilities are needed.
The center is therefore containing:
1. An adequate number of external telephones.
2. An adequate number of external telephones.
3. Wireless Set.
4. Plans of the factory to show :
(a) Areas of large inventories of hazardous materials including tanks, reactors, drums
and compressed gas cylinders.
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(b) Sources of sirens and safety equipments including fire, expansion, spill and gas
controls.
(c) Stocks of other fire extinguishing materials.
(d) The firewater system and additional sources of water.
(e) Site entrances and road system, updated at the time of the emergency to indicate
any road that is impassable.
(f) Assembly points, shelters, lunchroom and canteen.
(g) Casualty treatment centers first aid centers.
(h) Location of the factory in relation to the surrounding community (Annexure-2).
5. Nominal roll of employees, work permits, gate entries and documents for head count or
access to this information. Employee’s blood group information and address is
prepared and kept on Record.
Note pads, pens, pencils, rubbers, and stationary to record all messages received
and sent by whatsoever means.
More copies of this on –site and off- Site Emergency plan i.e. updated full text
including all Annexure. From this, some vehicle and messengers (runners) will be
kept ready at the center.
Troche, umbrella, rain – coats, and some extra sets of gas detectors explosive
meters and personal protective equipments.
Fire and Toxicity Control Arrangements:
Medical Arrangements:
A good organization should have, depending on size of the factory, its own ambulance room
or occupational health center or dispensary or hospital for medical. Names of surrounding
factories for mutual aid, list also the names and address of the surrounding hospital, nursing
homes, dispensaries etc. and give their details
6. Transport and Evacuation Arrangements:
In Major emergency, it will be necessary to evacuate personnel from affected areas and, as
a precautionary measure, to further evacuate non essential workers from areas likely to be
affected should the emergency escalate.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 686
We have separate evacuation alarm, which can be beard in 3 km radius. So that the people
be ready for evacuation. On evacuation, employee will be directed to predetermine
assembly points already explained earlier. If they are required to be evacuated outside the
factory and it a remote place, their transportation will be necessary which vehicles will be
required. At remote shelters their care and welfare will also be required. The safe
authorized passages / routes for escape is decided and marked by arrow in the plans as
explained in the details of emergency control Center.
Emergency Control Centre
Location of the centre: (1) Main ADM - Office ( 8.30 am to 5.00 pm ) (2). Main Gate Office after 5.00 pm
Telephone Nos. of the Centre Internal 4414 / 4446 Internal 4412 / 4403
External : 2676 : 247028 /
247283/247161
External : 2676 :247283/247161,
326606
Its period of operation Sr. No. Item kept in the centre see
(1) to (10)
Number or
quantity
Persons who will handle /
operate this item Last Present
Notes
1 2 3 4 5 6 7
01 phone & 1 Communication facility
02 Wireless
2 Safety Cupboard with some
PPE
1
3 Fire Extinguishers 2
4 Copy of On-Site Emergency
Plan
1
5 List of trained First Aider 1
6 Address & Telephone
Number of Key Personnel
1
7 Address & Telephone
Number outside Agencies &
Factories
1
8 Ambulance Van 1
9 Emergency Siren system 1
10 Emergency Light 1
Site Main controller /
Incident Controller
Security Officer , First Aid
Trained Persons & Time Keeper
Operation
During Mock
Drill
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
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6.2.3.7 FIRE CONTROL ARRANGEMENTS
6.2.3.7.1 FIRE FIGHTING, GAS LEAK CONTROL AND RESCUE OPERATION
A) Role of Manager (Fire and Safety) / Shift In-Charge (Fire & Safety)
1. Incident Controller will be the only person to direct the fire fighting and Emergency
operation.
2. Keep the constant touch with the SMC / In charge - EHS.
3. Direct the crew members to the scene of emergency and arrange replenishment of
Manpower / equipment / extinguishing media etc.
B) Role of EHS Representative:
1. On being notified about the location of fire/ gas leakage immediately proceed to the help.
2. Decide his line of action in consultation with Incident controller and take appropriate
measures to handle the emergency.
3. Assessing the severity of the incident immediately report to emergency controller about
the gravity of the situation.
4. He will assess the extra requirement required if any from the neighboring industry.
C) Fire crew members
1. On hearing fire alarm, emergency siren they shall immediately report to control room
and proceed to the scene of emergency and work under the direction of IC/ Dy IC.
2. The personal availability at the scene of incident to be made optimize.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 688
FIRE & TOXICITY CONTROL ARRANGEMENT
Fire Water :- Total Quantity - 500 M3 + Stand by 200 M
3
No. of Sprinklers : 02 Nos
No. of Monitors : 02 Fixed , 02 Trolley
Fixed Portable
Other
source &
capacity
No. of
hydrant
points
No. of
pumps,
type &
capacity
No. of
hose
reels &
total
length
No. of
fire
tenders
and
capacity Lifting
height Pressure
Lifting
height Pressure
Alternate
power
arrangement
1 2 3 4 5 6 7 8 9 10
10 meter 7
Kg/Cm2
- -
Own
Bore
well
45 Jockey,
Electrical
driven,
Diesel
pump
capacity
7 kg/hr
80 Nos.
of 15
mtrs cap
-
1 Nos DG Set
Dry Powder Type Foam Type Water Jet Products Other
Extinguishers
Personal Protective Equipment
No. of portable No. of portable Respiratory Non- respiratory Type of powder
& total quantity Extingui-
shes
Tonners
Type of
foam &
total
quantity
Exting. Tonners
No. of
size of
blankets
Other jet
products,
quantity
Type Number of
Quantity Type Nos. Type Nos.
12 13 14 15 16 17 18 19 20 21 22 23 24 25
1. DCP Powder 5
kg Cap. 10 kg
Cap.
Extinguishers
2. 150 kgs
storage
40 nos - AFFF
Compounds
1400 Ltrs
Carbo
25 nos - - - Co2 45 nos Self Contained
airline
breathing
apparatus
oxygen kit
Dust mask
7
10
2
150
Cartridge
Helmet
Gumboo
ts
Goggles
Appron
Chemical
Suits
Face
shield
50
100
50
50
20
15
15
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6.2.3.8 MEDICAL SERVICES
The roles of Medical officers are as follows;
(a) He will contact immediately to the SMC/IC.
(b) He will render necessary treatment, at Occupational Health Center.
(c) He will arrange for Hospitalization and Treatment at outside hospitals, if required.
(d) He will mobilize in getting the services of External medical agencies, other Para –
medical services etc. and transportation services etc.
(e) He will arrange for extra medical assistance/antidotes, from out, if required.
(f) He will arrange for first-aid trained volunteers for necessary help.
(g) He will liaise with the Government Health Authorities for treatment of the affected
persons nearby.
6.2.3.9 OTHER ARRANGEMENTS
Other arrangements include external transport, cranes, generator sets to supply emergency
power, environment monitoring equipment, rescue items etc. when available resources do
not meet the requirement.
STANDARD OPERATING PROCEDURE (EMERGENCY)
As soon as emergency alarm is heard, all essential workers shall report to IC or SMC.
They shall carefully listen to the instructions given by IC or SMC
According to the type of emergency/accident, they shall get equipped with PPE/Fire
fighting equipment and devices.
The runner among the workers shall inform SMC/IC and key personnel if they are not at
site.
The messenger amongst the workers shall deliver messages to nearby units as per the
instructions of SMC/IC.
The in-charge of medical arrangements shall prepare first-aid and other required
facilities for the injured.
The other essential workers shall try to control the emergency as per the instructions
given to IC.
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IC would keep SMC informed about the status of control measures being taken at the
site and ask for other requirements e.g. Mutual aid, equipment etc., if he find necessary.
SMC would co-ordinate with outside agencies regarding control measures being taken,
need for external help, evacuation, medical treatment etc.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 691
MEDICAL ARRANGMENTS
First aid Centers / Ambulance Room / OHC / Hospital Ambulance van or alternante arrangement
In charge person
Residence Sr.
No.
Name &
Location
Telex-
hone
Number Name &
Designation Phone Address
Facilities &
Equipments
Antidotes
avail-able
First
aiders
avail-
able
Accommodation Place of
availability Capacity
Facilities
in the
van
Driver’s
Name &
address
1 2 3 4 5 6 7 8 9 10 11 12 13 14
1 OHC -
Greentec
Chemicals
Pvt Ltd
Medical
Assistant
- Premises 01
Ambulance
Van 01 Bed,
Oxygen
Cyl.,
Structure,
Artificial
breathing
apt,
Balance, B P
Meter,
Yes Yes ,
Trained
First
Aider
Available
round
the clock
Yes Main Gate
OHC
building
6 Oxygen
kit, First
Aid bod,
Structure
Driver
available
at Main
Gate
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
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6.3 COMMMUNICATION SYSTEM
After the assessment of risk & their possible environmental impact and after making an
organization for the preparedness to control the emergency, the next most essential step is to
make us ready for Communication at the time of emergency. Communication System is a
Crucial Factor while handling emergency.
Company will have quick & effective Communication System through which, any situation,
which can lead to emergency, can be informed or known to.
i. All working inside the plant.
ii. Key Personnel outside during normal working hours & during off-duty hours.
iii. Outside emergency services, Statutory and Local Authorities and
iv. Neighboring facilities and public leaving in vicinity.
Each and every section, Plant & Department of the Factory shall be connected by internal
telephones. External Phone at Office and Residence and Mobile shall be also available with
Key Personnel and top executive of the factory. Hot lines shall be provided with mutual aid
Partner through the Emergency Control Center. The Communication System begins with
raising the alarm declaring the emergency, Telephone messages and Procedure to
communicate the emergency to other persons & General Public.
6.3.1 RAISING THE ALARM
As soon as incident takes place inside the factory and is noticed by someone, the first step is
to raise the nearest manual emergency bell to alert the nearby people. Next, he/she
informs the security persons to raise the emergency siren located at the factory gate. The
security personnel sound the siren, raising and lowering the sound three times in a 10
second “ON”, 5 second “OFF” sequence. After emergency is over “CLEAR SIREN”, 30
seconds. All the security employees shall be trained for operating the siren to announcing
the emergency. In case of power failure, manual bell shall be also provided.
The alarm sound informs the I.C and the S.M.C that an emergency has been created and
emergency organization is to be activated. The I.C. rushes to the site and takes charge of
the scene.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
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ALARMS & SIRENS
Plant wise alarm points Sound difference if any Sr.
No.
Plant / Dept./ Location Sr. No
.of
Its place
of
Type of
the
Its period
The alarm
(signal)
Type of Type of
alarm
Duration
of
Type of
sound
1 2 3 4 5 6 7 8 9 10 11 12 13
1 At the
Main
gate
- - 1 At
Security
Gate
Electric Once in a
week/Every
Monday at
10-30 AM
Whole
complex
and
surrounding
area
Fire, Toxic,
Emergency
Release All
clear
2 Fungicide
plant
- - 1 Fungicide
plant
Electric Once in a
week/Every
Monday at
10-30 AM
Entire
Factory
Fire, Toxic,
Emergency
Release All
clear
As per attached siren code
# Public Announcement System Available at ECC / Main Gate for emergency communication and speakers are available in factory premises
as well as offices for fast communication.
.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 694
6.3.2 DECLARING THE MAJOR EMERGENCY
Major emergency has to be declared after sufficient and through check because the
declaration of major emergency puts many agencies on action and it may disturb the
running system, which may be Costly at, time or its Consequence may be Serious. Therefore
major emergency must not be decided on whims or immature judgment or without proper
thought. Looking to all the above, we will have taken care to nominate the persons who can
declare the emergency; we will have selected them on the basis of their knowledge &
experience. These persons will be technically qualified and experienced. They shall advice
the Incident Controller or Site Main Controller regarding the type of emergency. On being
convinced, the Site Main Controller or Incident Controller shall declare an ON-SITE
emergency. The decision about major emergency shall be taken as early as possible and
without wasting time so that control action can be started immediately.
6.3.3 TELEPHONE MESSAGES
After hearing the emergency alarm and during emergency or even while just receiving the
emergency message on phone, Telephone operator should be precise, sharp, attentive and
quick in receiving and noting the message and subsequently effective in further
Communication A form to record emergency telephone calls shall be available with
telephone operator or Person available in Emergency Control Center, who has to record
such calls during emergency. Telephonic messages shall be given out by the telephone
operator to Site main Controller and key personnel as per the instructions of the Incident
Controller. Telephonic messages shall also be given to authorities and external agencies to
describe the type of emergency. All details of emergency shall be collected/delivered
according to this format shall available with the telephone operator.
6.3.4 COMMUNICATION OF EMERGENCY & STATUTORY INFORMATION
6.3.4.1 COMMUNICATION OF EMERGENCY
An effective system to communicate emergency shall be available.
Inside the factory i.e. workers including key personnel and essential workers, on duty &
inside during normal working hours.
To key personnel and essential workers not on duty and outside during normal working
hours.
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Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 695
To the outside emergency services and the Government authorities.
To the neighboring factory & the General Public in the vicinity.
a) Information to Workers
All personnel inside the factory shall be informed by the sounding of the siren or in case of
electricity by ringing the bell.
b) To key personnel outside during normal working hours
The key personnel outside the factory premises shall be informed as per the need by
external telephones or runners.
c) To the outside Emergency Services and the Authorities
Once the emergency is declared, it is essential that the outside emergency services should
be informed in the shortest possible time. Responsibilities shall be fixed as per the
Incident/Emergency Command structure/plan to contact outside agencies for help and to
communicate to the all the Government and other Authorities such as Fire Brigade, Police,
District Emergency Authorities, Factory Inspectorate & Hospital etc. In case of major
emergency, outside agencies like mutual aid, hospitals, policies, Factory Inspector, Collector,
Fire-brigade etc. shall be informed by telephone or by sending special messenger from
emergency control center.
d) To neighboring factories and the General Public
A major emergency will affect areas outside the works and it is essential that neighboring
factory and General Public, should be informed to enable them to take prompt action to
protect their own workers and to take whatever measures may be possible to prevent
further escalation of the emergency due to effects on their own installations, at the same
time, they may be able to provide assistance as part of a prearranged mutual aid plan.
Further responsibilities shall be fixed to inform the neighboring factories and the General
Public leaving in the vicinity. The neighboring units shall be informed about an emergency
through external telephones or runners. The general public shall be informed about an
emergency using loudspeaker on scooter or rickshaw or car. Help from police shall be
sought if required.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 696
6.3.4.2 STATUTORY INFORMATION
a) Information to Workers
Set of Statutory information regarding types of hazards and their prevention and control as
directed in the Factories Act shall be prepared by the unit. This information shall be printed
in the local language and given in the form of booklet to all workers including contract
workers.
b) To the outside emergency services and authorities
Statutory information in the form of booklet shall be given to outside emergency services
and authorities.
c) To neighboring firms and the general public
Statutory information in the form of booklet will be given to neighboring units and the
general public of the villages in the vicinity of the unit.
6.4 ACTION ON SITE
The activities related to emergency time activities shall be divided into two parts. These are
Pre-emergency activities
Post-emergency Activities
6.4.1 PRE-EMERGENCY ACTIVITIES
6.4.1.1 INTERNAL SAFETY SURVEY
A safety committee shall be constituted as per Factories Act. The nominated members of
the committee shall be assigned the responsibility to conduct safety survey once in a month
before safety meeting. The internal safety survey includes –
Identify various hazards in the factory
Check whether protective equipments are in sound working condition
Check various safety installations located at various plants for proper working
Check sprinklers, showers, etc. in all plants
Suggest extra modifications/ requirements to make systems more reliable
Check presence of toxic gases by the help of dragger tube
Frequency of Internal Safety Survey: Once in a month
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 697
6.4.1.2 THIRD PARTY SURVEY
A safety survey shall be carried out once in a year by an external agency. It shall include –
Inspection of building, structures for strength and stability
Identify and study the hazards inside individual plants and within the factory
premises.
Check safety system for its adequacy.
Suggest modifications or additions in the operating practices and safety system, if
necessary.
Frequency of Third Party Safety Survey: Once in a year
6.4.1.3 PRESSURE VESSEL TESTING/ EXAMINATION
To prepare list of pressure vessels in the plant with details of operating conditions
and manufacturing details.
To carry out preventive maintenance of valves & fittings on all pressure vessels
(valves, pipelines, pressure gauge, temperature recorders and emergency vent lines)
To arrange for testing and examination of all pressure vessels as per the rules of
Factories Act by govt. certified competent person on due date.
To maintain record of testing and certificates issued by competent person and make
them available to Factory Inspector at the time of inspection.
Frequency of Pressure Vessel Testing / Examination: Twice in a year
6.4.1.4 NON-DESTRUCTIVE TESTING (NDT)
To prepare list of equipment and pipelines in the plant which require NDT as per the
rules of Factories Act?
To arrange for Non-Destructive Testing (NDT) as per the rules under Factories Act by
govt. certified competent person on due dates.
To maintain record of testing and certificates issued by competent person and make
them available to Factory Inspector at the time of inspection.
Frequency of Non-Destructive Testing : Once in a year
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 698
6.4.1.5 SAFETY RELIEF VALVES TESTING
To prepare list of Safety Relief Valves installed on various equipment and pipelines in
the unit along with detailed specifications.
To prepare schedule for testing and calibration as per the rules under Factories Act
by govt. certified agencies on due dates.
To maintain record of testing and certificates and mark dates of testing and
calibration on the valves.
To carry out repairs/replacement as suggesting by the testing authority.
Frequency : Twice in a year
6.4.1.6 FIRE SYSTEM TESTING
To prepare list of various fire-fighting equipment (Fire Extinguishers, etc.) installed at
various locations in the unit along with detailed specifications.
To prepare schedule for testing of all these equipment and check operability
To maintain record of testing and mark dates of testing on the equipment.
To carry out repairs/replacement of defective equipment
Frequency: Once in a month
6.4.1.7 MUTUAL AID SCHEME
To prepare Mutual Aid Scheme and enter into agreement with the neighboring units
for getting or extending help during emergency
To appoint coordinator for follow-up under mutual Aid Scheme
To review the scheme once in a year with coordinators of neighboring units w.r.t.
scope of help, type of aid, contact persons, etc.
To include the scheme in mock drills
6.4.1.8 MOCK-DRILLS
To conduct minor mock drills to train employees about their role / duties during
emergency
To refresh training to the employees for fire fighting, spill control, use of personal
protective equipments etc.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 699
To check whether various members of emergency control committee remember
their role / duties properly and to find out the faults and points of improvement in
their performance.
To check whether the various equipment for emergency control are operating
satisfactorily and find and rectify the draw-backs if any.
To conduct major mock-drills with permission from the authorities
Mock drills shall be regularly conducted in our unit by our Emergency Control Organization
and the findings are compiled to analyze whether employees are familiarized with the
emergency control procedures and what sort of training is required to be given.
6.4.1.9 SAFETY TRAINING
To organize regular training for the employees for handling of safety equipment, use of
personal protective equipment, first-aid, etc. by internal/external faculty, as well as by
sending persons outside to attend safety programs etc. The topics covered in safety
training will be –
Training on fire fighting
Training on spill control
Training on toxic release control
Training on good housekeeping
Training on use of PPE
The records of the training programs shall be maintained by the Safety Committee. New
topics will be included in the safety training programs year by year to upgrade safety
knowledge among the workers.
Frequency: Once in a year
6.4.1.10 PERSONAL PROTECTIVE EQUIPMENT
To procure adequate number of personal protective equipment (aprons, hand
gloves, safety goggles, helmets, nose masks, safety belts, gas cartridges, self-
breathing apparatus, safety shoes etc.) suitable for plant operations and maintain
records of use.
To have proper system for issuing the PPE and disposal of used PPE
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 700
To train the workers about proper use of PPE.
To check the fresh air blowers provided at confined spaces for fresh air to workers.
6.4.1.11 COMMUNICATION
To maintain internal/external telephones in working order
To check alarms / siren / loudspeakers for workability
To provide manual emergency bells at various location for use during power failure
To periodically check wind cock for wind direction
To check lightning arrestors installed at different locations for physical condition and
proper earthing connection.
6.4.1.12 EMERGENCY LIGHTS
To keep sufficient number of emergency torch/ batteries in ECC as well as at the
production site
To maintain the three DG sets available in the factory as stand-by for power failure.
The D.G. sets are set to start functioning within two minutes of failure of electricity.
6.4.1.13 EMERGENCY CONTROL ROOM
It is necessary to maintain the Emergency Control Room and keep it equipped with all
necessary items, documents, telecommunication systems, PPE etc. required in case of an
emergency.
6.4.1.14 ASSEMBLY POINTS
To fix assembly points in the factory for non-essential workers
To fix assembly points for plant emergency staff and coordinators
To maintain record of no. of workers gathered at the assembly points at the time of
emergency. The Safety Committee shall nominate a person for this duty.
6.4.1.15 LIAISON WITH STATE AUTHORITIES
To liaison with civil authorities, local hospitals, Fire-Brigade, Collector, factories
Inspector, Police, etc regarding emergency activities and need for external aid.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 701
To keep the details regarding name, address & telephone numbers of various govt.
authorities and neighboring units available and update the details from time to time.
To inform about Mock-drill in advance and if required conduct mock-drill in presence
of any of these authorities.
To submit report of Mock-drill conducted and the out comings with photograph to
Factories Inspector.
6.4.1.16 HOSPITAL FACILITIES
To equip Occupational Health Centre with First-Aid and medicines
To keep Health records (esp. blood-group records) of all employees
To liaison with hospitals in the area of the unit
To keep list of blood donors ready for reference
To update arrangements with neighboring units for emergency first aid.
6.4.1.17 OUTSIDE SHELTER
To reserve space in nearby schools/hospitals/buildings for temporary shelter during
emergency
To arrange for clothing, food, medicine in temporary shelter
6.4.1.18 STATUTORY INFORMATION
Statutory Information about chemicals handled in the unit, manufacturing process, the
hazards in the unit, methods of prevention and control, first aid measures etc. shall be given
to
- Workers
- Public and Neighboring units
- Government authorities & outside emergency services
6.4.1.19 PROTECTIVE DEVICES & ENGINEERING MAINTENANCE
Installation of safety valve and pressure gauges on vessels used for high pressure
operations.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 702
Installation of temperature indicators on reactors, temperature switch or alarm at
critical reactors
Maintenance of cooling water systems and pumps. To keep standby pump at cooling
tower.
Installation of overhead water tank for emergency. To keep it filled and regular
cleaning of the same
Periodic cleaning of heat transfer surfaces (jacket, reactors, shell & tube heat
exchangers, boilers)
To keep minimum inventory of hazardous materials with records
To maintain good housekeeping and ensure safety compliance
6.4.1.20 LIST OF SUPPLIERS OF SAFETY EQUIPMENT
To prepare and preserve list of suppliers of safety equipment e.g. first aid box,
medicines, fire extinguishers, PPE, communication, self breathing apparatus, chlorine
kit, etc.
To check all supplies every three months
To update the list and keep it ready-to-refer location in the plant as well as at ECC
6.4.1.21 FIRE PREVENTION PLAN
List of major work-place fire hazards
Potential ignition sources
Sparks from electrical fitting / motors
Sparks from welding operations
Ignition system of boiler house
Sparks from static electricity
Fire prevention & control measures
Use of flameproof electrical fittings and electric motors wherever necessary
No welding shall be done anywhere in the plant without prior permission from safety
officer and necessary precautions from in charge of the area.
Ignition system of boiler should be provided with guard
All vessels and pipeline should be properly earthed to prevent static electricity
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 703
The vent lines of all vessels and tanks holding flammable materials should be
provided with flame arrestors
Fire extinguishers shall be provided at all critical locations in the unit
6.4.2 POST EMERGENCY ACTIVITIES
These activities are to be carried out after an emergency is over so as to establish the cause
of the emergency and decide the measures to be taken to prevent its re-occurrence. These
activities are –
1. Collection of records of accident, injury, damage to property, buildings, equipment,
material and loss of production
2. Conducting enquiries and concluding preventive measures
3. Making insurance claim for the materialistic loss / damage
4. Implementation of enquiry report’s recommendations
5. Rehabilitation of affected persons within and outside the plant
6. Restarting the plant and normalizing the operations.
6.4.3 EMERGENCY TIME ACTIVITIES
The probable emergency situation that can arise in the unit and the corresponding control
actions are describes below.
6.4.3.1 FLAMMABLE RELEASES
Source / Incident – Fire involving spilled combustible material near or in flammable storage
areas
Control action –
1. Any one who notices fire shall sound emergency alarm.
2. SMC/IC who is at site, shall immediately rush to the scene and assess the situation.
For fire due to spillage of combustible material, he activates the on-site plan as -
He cuts off electric supply to that area and evacuates all the persons to safe
assembly points.
He calls in DIC (if DIC is not present there) and asks essential workers to fight fire
with dry chemical / CO2 fire extinguisher or sand.
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Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 704
He inform fire brigade telling them in briefly about kind of fire and type of
extinguishers required
He informs mutual aid teams and asks for necessary help.
He arranges first-aid / hospitalization for the affected persons.
Fire officer on reaching the site, takes charge of the fire-fighting operations
Mutual aid teams shall be asked for help in the form of first-aid, transport etc.
If fire is growing, fire officer informs IC who alerts neighboring units and through
SMC gets more fire-fighting help.
Fire fighting shall be continued till fire is fully overcome
After extinguishing fire, fire officer cools the entire area with water spray and checks
that no re-ignition shall be likely. After that, he declares the area safe.
IC tells essential workers to sound all clear
The incident shall be recorded
SMC arranges to inform families / relatives of injured / dead.
SMC issues authorized statement to press / media.
SMC informs Factories Inspector about the incident and related information
6.4.3.2 TOXIC RELEASES
Source / Incident – Pressure release due to failure of
- Stuffing box gland packing
- Pressure release valve
- Vessel / pipeline failure
- Cylinder/tank/drum leakages like Cl2/Bromine/Thinonyl chloride
Control action –
1. Any one who notices the release shall sound emergency alarm.
2. Leakage - kits /minimum stock /spare tank
2. SMC/IC who is at site, shall immediately rush to the scene and assess the situation.
For toxic release from a reactor, he activates the on-site plan as -
He evacuates all the persons to safe assembly point.
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He calls in DIC (if DIC is not present there) and asks essential workers to wear self-
breathing apparatus and if the reaction is exothermic, start cooling water flow in the
reactor jacket and cool the reactor as soon as possible.
The essential workers stop all the charging pumps of that reactor and the nearby
reactors.
He informs mutual aid teams and asks for necessary help.
He arranges first-aid / hospitalization for the affected persons.
Mutual aid teams shall be asked for help in the form of first-aid, transport etc.
When the leak stops and the air shall clear of toxic release, IC tells essential workers
to sound all clear.
The vessel / rupture disc/gland packing will be attended by maintenance
department.
The incident shall be recorded
SMC arranges to inform families / relatives of injured / dead.
SMC issues authorized statement to press / media.
SMC informs Factories Inspector about the incident and related information
6.4.3.3 CHEMICAL SPILL
Most of the storage tanks shall be located in Storage Tank Yards. Dyke walls of sufficient size
will be connected around the tank yard. Neutralizing material shall be kept nearby. For
dilution, water connection will be provided on all sides of tank farms. Sand buckets shall be
provided for covering spillage of flammable / corrosive materials.
6.4.4 EVACUATION & TRANSPORTATION
All non-essential workers shall be evacuated from incident area and adjacent areas to safe
assembly points. Assembly points shall be clearly marked and assembly point in-charge will
also be designated. The assembly point in-charge will be a well-trained supervisor who shall
keep record of persons arriving at the assembly point and direct them for proper gathering.
He shall also inform the ECC about the persons gathered at the assembly point. Those in
need of medical treatment shall be transported to first-aid center / hospital as the case may
be. In case of major emergency all non-essential workers shall be transported to temporary
shelter.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 706
6.4.5 SAFE CLOSE-DOWN
As per the instructions from IC or SMC, some parts or full of the plant shall be closed down
by the essential workers. The procedure for safe shut-down and start-up will be given in
safety manual given to all workers.
6.4.6 USE OF MUTUAL AID
Mutual aid from neighboring units shall be called up as and when required. The aid shall be
taken under the supervision of SMC.
6.4.7 HELP OF EXTERNAL AUTHORIES
Outside authorities such as Police, District Emergency Authority (DEA), Factory Inspector,
Disaster Management Centre, GIDC officer, Industries Association, Regional Pollution
Control Board, nearby hospitals etc. shall be informed of the on-site and off-site emergency
plans and called in as per need.
6.4.8 MEDICAL TREATMENT
Injured workers shall be located and given prompt first-aid by essential workers and key
personnel. Those requiring medical treatment shall be taken to the hospital / outside
medical center.
6.4.9 ACCOUNTING FOR PERSONNEL
Through daily muster rolls and with the help of shift-in-charge the head count shall be
undertaken to find out whether persons are missing and if so immediate search shall be
carried out to locate them. The list shall include company employees, contract workers as
well as visitors. Help from local authority or fire-brigade shall be taken if required. This list
shall be kept with time keeper / security officer at any time and shall be used to account for
personnel. Injured shall be taken to hospitals and their families/relatives shall be informed
Casualties would be identified, their families and local authority shall be informed.
6.4.10 ACCESS TO RECORDS
In order to inform families/relatives of injured/dead, a up-to-date list of names and
addresses of all the workers is maintained in addition to the muster roll where shift-wise
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 707
attendance is marked. Such list includes health records. This list will be available at the ECC
and one such copy shall be available at our head office.
6.4.11 PUBLIC RELATIONS
Our General Manager shall be the only nominated person to issue administrative statement
about the accident or emergency to news/media. No other person shall divulge any
information to any news / media person.
6.4.12 REHABILITATION
In case of Toxic release or chemical spillage, Senior Fire Brigade Officer would ensure that
the incident area shall be safe and cleaned up of all mess. Then only, he would allow people
to re-enter the location. In case of fire, the Senior Fire-Brigade Officer shall ensure that the
area is cooled down and there are no chances of re-ignition. IC shall arrange for clean-up of
the area and then only people shall be allowed to re-enter the area for work. Even when all
clear has been given, great care shall be taken when re-entering affected areas and no work
in connection with the salvage, collection of evidence or start up shall be taken up until a
thorough examination of the area has been carried out. The statutory powers of the
Factory Inspector shall be kept in mind before any evidence is disturbed. Particular care
shall be taken to avoid the introduction of possible sources of ignition, such as diesel
engines, hand or power operated tools, flame cutting equipment, etc. until it has been
established that no flammable materials are present where they could be ignited.
6.5 OFF – SITE EMERGENCY PLAN
6.5.1 NEED OF THE OFF – SITE EMERGENCY PLAN
An off-site emergency plan is prepared to deal with those incidents which have the potential
to harm persons or the environment outside the boundary of the factory premises. A major
accident, major emergency and disaster may affect areas outside the plant. An explosion
can scatter debris over wide areas and its effects of blasts can cover considerable distances.
Wind can spread burning fumes of toxic gases. Thus the events like these described above
can affect outside areas and combating them needs an Off-site Emergency plan.
Envisaging such a rare incident, an off-site emergency plan should be drawn up for the
following purpose.
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1. To provide basic information about the risk and environmental impact assessment
related to the unit to local / district authorities, police, fire-brigade, surrounding
units, and the general public. To appraise them of consequences and the protection
/ prevention measures and control actions and to seek their help to communicate
with public in case of a major emergency. The information from all industries shall
enable district authorities to educate public about what could go wrong, and to train
them of measures to be taken as an individual.
2. To enable district authorities to prepare the off-site emergency plan (contingency)
for the district or particular area and to organize rehearsals and initiate actions
learnt from these incidents.
Our Emergency Plan shall be made after considering the all possible effects of incidents on
the neighboring population and the remedial measures will be devised in consultation with
the local authorities and emergency services.
6.5.2 STRUCTURE OF THE OFF-SITE EMERGENCY PLAN
Organization Details of :
Command Structure, Co – Ordination arrangements, warning systems,
implementation procedures, emergency control centers.
Name & appointments of :
Incident Controller, Site Main Controller, their deputies and other key personnel.
Communication Identification of personnel involved, communication center, call signs, network, lists
of key telephone numbers.
Specialized emergency
equipment
Details of availability and location of :
Heavy lifting gear, bulldozer, specialized fire fighting equipments, fire boats.
Specialized Knowledge Details of specialized bodies, firms and people upon whom it may be necessary to
call, egg, people or firms with specialized chemical knowledge, laboratories.
Voluntary Organizations Details of organizers, telephone numbers, resources, etc.
Chemical Information Details of the hazardous substances stored or processed on each site and a summary
of the risks associated with them. (HAZCHEM details).
Meteorological
Information’s
Arrangements for obtaining details of weather conditions prevailing at the time and
for weather forecasts.
Humanitarian
arrangements
Transport, evacuation centers, emergency feeding, treatment of injured – first aid,
ambulance, temporary mortuaries.
Public Information Arrangements for
(a) Dealing with the media, press and office.
(b) Informing relatives etc.
Assessment Arrangements for
(a) Collecting information on the cause of the emergency appointment of a
historian.
(b) Reviewing the efficiency and effectiveness of all aspects of the emergency
plan.
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
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6.5.3 ROLE OF FACTORY MANAGEMENT
The Off-Site emergency Plans are dovetail so that the emergency services shall be
summoned at the appropriate time and shall be provided with accurate information and a
correct assessment of the situation. The responsibility for this is with the Site Main
Controller. The Site Main Controller shall provide a copy of our On-Site and Off-Site
Emergency Plan to the District authorities, the Factories Inspectorate and the Emergency
Services, so that on the basis of information and such authorities can make their emergency
preparedness plan to formulate and execute the District / Area off Site Emergency Plan.
Further on the advice of the authorities we can also modify our plan to make our plan more
effective and perfect.
6.5.4 ROLE OF EMERGENCY CO-ORDINATION OFFICER (ECO)
The various emergency services will be co-ordinated by the Emergency Co-ordination officer
(ECO), who will likely to be a Collector. The ECO will liaise closely with the Site Main
Controller. The Emergency Control Centre of the factory can be utilized by the ECO to keep
liaison with the Site Main Controller.
6.5.5 ROLE OF THE FIRE AUTHORITIES
The control of fire is normally the responsibility of the senior fire officer who would take
over the handling of fire from the IC on arrival at the site.
The senior fire brigade officer may also have similar responsibility for other events
such as explosion and toxic releases. Fire authority having major hazard units in the
area shall- Familiarize themselves with the location and site of all stages of
flammable materials, water and foam supply points, fire fighting equipment.
Act as observer of an on-site exercise involving only site personnel
6.5.6 ROLE OF THE HEALTH AUTHORITIES
Health authorities, including Doctors, Surgeons, Hospitals, and Ambulances so on, have a
vital part to play following a Major Accident and they should form an integral part of any
emergency plan. In case of major fires, injuries will be the result of the effects of thermal
radiation to a varying degree, and the knowledge and experience to handle this type of
injuries cases may be generally available in most of the hospitals. But in case of major toxic
M/s. GREENTEC CHEMICALS PVT. LTD. ENVIRONMENT IMPACT ASSESSMENT REPORT
Prepared By: Aqua-Air Environmental Engineers Pvt. Ltd., Surat 710
releases, the effects vary according to the chemical, which has leaked, and it is important for
health authorities that might be involved in dealing with the aftermath of a toxic release to
be familiar with the treatment appropriate to such casualties. Major Off-Site incidents are
likely to require medical equipment and facilities additional to those available locally and a
Medical 'Mutual Aid' scheme should exist to enable the assistance of neighboring
authorities to be obtained in the event of an emergency.
6.5.7 ROLE OF TELEPHONE DEPARTMENT
The communication system between the factory and the various above role-playing
authorities must be effective. The ineffective public telephone system will not be useful in
emergency. Therefore, telephone department should maintain the phones and if required
temporary telephone connection may be provided to various above authorities to deal the
emergency.
6.5.8 ROLE OF POLICE AND EVACUATION AUTHORITIES
To protect life and property
To control traffic movement
To inform people to remain indoors or evacuate
To carry-out evacuation
To identify dead, deal with casualties and inform relatives of dead or injured.
For evacuation, the following criteria are useful:
a) In case of major fire, only houses close to fire and in the direction of smoke need
evacuation
b) If fire is escalating and in turn threatening a store of hazardous material, it is
necessary to evacuate people nearby if time is available; otherwise they should be
informed to keep themselves indoor and shield from the fire.
c) For release of toxic gases, limited evacuation may be appropriate in downwind
direction with windows closed and provides good protection. Toxic gases which are
hazardous down to much lower concentration cover a long distance. This factor
must be considered while deciding upon the need and extent of evacuation.
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6.5.9 ROLE OF THE MUTUAL-AID AGENCIES
Mutual-aid arrangements shall be made in areas of fire & toxicity control, medical and
transport & evacuation. All partners of mutual-aid shall extend all possible help in these
areas.
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6.6 OCCUPATIONAL HEALTH AND SAFETY
For large industries, where multifarious activities are involved during construction, erection,
testing, commissioning, operation and maintenance; the men, materials and machines are
the basic inputs. Along with the boons, industrialization generally brings several problems
like occupational health and safety. The industrial planner, therefore, has to properly plan
and take steps to minimize the impacts of industrialization and to ensure appropriate
occupational health and safety including fire plans. All these activities again may be
classified under construction and erection, and operation and maintenance.
6.6.1 OCCUPATIONAL HEALTH
Occupational health needs attention both during construction & erection and operation &
maintenance phases. However, the problem varies both in magnitude and variety in the
above phases.
6.6.1.1 CONSTRUCTION AND ERECTION
The occupational health problems envisaged at this stage can mainly be due to
constructional accident and noise. To overcome these hazards, in addition to arrangements
to reduce it within TLV's, necessary protective equipments shall be supplied to workers.
6.6.1.2 OPERATION AND MAINTENANCE
The problem of occupational health, in the operation and maintenance phase is primarily
due to noise which could affect consultation. The necessary personal protective equipments
will be given to all the workers. The working personnel shall be given the following
appropriate personnel protective equipments.
Industrial Safety Helmet;
Face shield
Zero power plain goggles with cut type filters on both ends;
Zero power goggles with cut type filters on both sides and blue color glasses;
Welders equipment for eye and face protection;
Cylindrical type earplug;
Ear muffs;
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Canister Gas mask;
Self contained breathing apparatus;
Leather apron;
Aluminized fiber glass fix proximity suit with hood and gloves;
Boiler suit;
Safety belt/line man's safety belt;
Leather hand gloves;
Asbestos hand gloves;
Acid/Alkali proof rubberized hand gloves;
Canvas cum leather hand gloves with leather palm;
Lead hand glove;
Electrically tested electrical resistance hand gloves; and
Industrial safety shoes with steel toe.
6.6.1.3 HOSPITAL FACILITIES
It is proposed that client will make formal agreements with nearby hospital having facilities
to attend fire and toxic effect cases for attending the affected persons in the emergency
arising out of accidents, if any.
6.6.1.4 FACTORY MEDICAL OFFICER
A qualified doctor will be appointed as FMO on retainer ship basis. Apart from him,
Paramedical Staff will be employed.
6.6.1.5 PROPOSED FACILITY TO BE MADE AVAILABLE AT OHC
One Room is proposed to be provided to be operated as OHC. The centre will be equipped
with following medical equipments:—
1. Examination Table
2 Dressing Tables For performing Dressing
3. Glucometer For measurement of Blood Sugar
4 Vision chart To evaluate vision acuity
5. Nebuliser For relieving coughs & Breathing Difficulty
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6. Infra red light for relieving muscular pain
7. Suction machine For cleaning airway
8. Autoclave machine For sterilizing cotton &dressing material
9. Weighing Machine For measuring body weight
10. Medical Oxygen Cylinder kit
11. Sphygmomanometer To measure blood pressure
12. Refrigerator To preserve medicines
13. Thermometer
OHC (OCCUPATION HEALTH CENTRE)
Item Quantity
First aid boxes 15 Nos
Stretchers 03 Nos
Ambulance 01 No + other vehicles
Availability of Doctors/nurses 02 Nos FMO & (01 Medical Asst.)
Availability of medicines/antidotes Yes , All relevant chemicals
Dr Consulting room 13 * 13 sq ft area
No. of beds in Medical Room 02 Nos ( 27 * 13 sq ft area )
Details of other facilities/equipment OHC related all medical facility &
Mutual Aid facility,
Medical Oxygen cylinders – 03 Nos
Freeze – 01 no
Nebuliser – 01 no
Dressing equipments
Peak flow meter – 01 no
B. P. Meter
Ambush bag
Digital thermometer
Medical Examination Every six month as per Hazardous process
Annually as details examination
Medical record keeping As per GFR Form – 32 & From – 33
6.6.1.6 AMBULANCE VAN
An ambulance van is proposed to be made available 24 hours at Fire Station.
6.6.1.7 FIRST AID BOX
First Aid Boxes are proposed to be made available at the different location in the plant,
Training to be given to employees for First Aid.
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FIRST AID BOX (LIST OF MEDICINES)
SR.
NO.
NAME OF MEDICINE
1 Tab. Crocin
2 Eno Powder
3 Iodine Tincture
4 Savlon / Dettol
5 Tube Soframycin
6 Tube Burnol
7 Eye drop –Locula 10% / Gentamacin
8 Bandage roll
9 Cotton
6.6.1.8 PERIODIC MEDICAL EXAMINATION
It is proposed that client will ensure that…
(1) Workers employed shall be medically examined by a qualified medical practitioner/
Factory Medical Officer, in the following manner:
(a) Once in a period of 6 months, to ascertain physical fitness of the person to do the
particular job;
(b) Once in a period of 6 months, to ascertain the health status of all the workers in
respect of occupational health hazards to which they are exposed and in cases where
in the opinion of the Factory Medical Officer it is necessary to do so at a shorter
interval in respect of any workers;
© In periodic and pre-medical examinations, various parameters will be checked. Viz.,
LIVER FUNCRION TESTS, Chest X-rays, Audiometry, Spirometry, Vision testing (Far &
Near vision, color vision and any other ocular defect) ECG and other parameters as will
be found necessary as per the opinion of Factory Medical officer.
(2) No person shall be employed for the first time without a certificate of granted by the
Factory Medical Officer.
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6.6.1.9 EMP FOR THE OCCUPATIONAL SAFETY & HEALTH HAZARDS SO THAT SUCH
EXPOSURE CAN BE KEPT WITHIN PERMISSIBLE EXPOSURE LEVEL (PEL)/THRESHOLD
LEVEL VALUE (TLV) SO AS TO PROTECT HEALTH OF WORKERS
1. It is proposed to formulate and implement an EMP for Occupational Safety and
Health with following aims…
To keep air-borne concentration of toxic and hazardous chemicals below PEL
and TLV.
Protect general health of workers likely to be exposed to such chemicals
Providing training, guidelines, resources and facilities to concerned
department for occupational health hazards.
Permanent changes to workplace procedures or work location to be done if it
is found necessary on the basis of findings from workplace Monitoring Plan.
2. It is proposed that this EMP be formulated on the guidelines issued by Bureau of
Indian Standards on OH&S Management Systems: IS 18001:2000 Occupational
Health and Safety Management Systems
3. Proposed EMP will be incorporated in Standard Operating Procedure also.
4. The proposed EMP will also include measure to keep air-born concentration of
toxic and hazardous chemicals below its PEL and TLV, like…
a. Leak Surveys
b. Separate storage for toxic chemicals
c. Exhaust Ventilation
d. Proper illumination
e. On-line detectors toxic chemicals
f. Close processes to avoid spills and exposures
g. Atomization of process operations to hazards of manual handling of
chemicals
h. Supply of proper PPEs like Air mask, Berating canisters, SCBA sets, On-line
breathing apparatus at the places where there is possibility of presence of
toxic chemicals
i. Decontamination procedure for empty drums and carboys.
j. Regular maintenance program for pumps, equipment, instruments handling
toxic and corrosive chemicals
k. Display of warning boards
l. Training to persons handling toxic and corrosive chemicals
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5. Workplace Monitoring Plan
It is proposed that a Workplace Monitoring Plan to be prepared & implemented in
consultation with FMO and industrial hygienists.
Each workplace must be evaluated to identify potential hazards from toxic
substances or harmful physical agents. Air-borne concentration of toxic chemicals
will be measured and record will be kept.
The current state-of-the-art exposure measurement model is as follows: For
purposes of measuring worker exposure across a single shift it is sufficient t o place a
reasonably accurate exposure measuring device on the worker , within t he worker ’s
breathing zone, and have it operate for nearly the full shift. Client has been proposed
to study the exposure data when the plant is operative.
6. Health Evaluation of Workers
1. It is proposed that management will device a plan to check and evaluate the
exposure specific health status evaluation of workers
2. Workers will be checked for physical fitness with special reference to the possible
health hazards likely to be present where he/she is being expected to work before
being employed for that purpose. Basic examinations like Liver Function tests, chest
x ray, Audiometry, Spirometry Vision testing (Far & Near vision, color vision and any
other ocular defect) ECG, etc. will be carried out. However, the parameters and
frequency of such examination will be decided in consultation with Factory Medical
Officer and Industrial Hygienists.
3. While in work, all the workers will be periodically examined for the health with
specific reference to the hazards which they are likely to be exposed to during work.
Health evaluation will be carried out considering the bodily functions likely to be
affected during work. The parameters and frequency of such examination will be
decided in consultation with Factory Medical Officer and Industrial Hygienists. Plan
of monthly and yearly report of the health status of workers with special reference to
Occupational Health and Safety.
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Occupational health impact on employees, control measures, action plan if accident occur Sr.
No.
Chemical Occupational health impact
on
Employees
EMP/Measures to keep
exposure below
TLV/ PEL
EMP for STEL & IDLH
1 Acetonitrile
Potential Acute Health
Effects: skin contact
(irritant), of eye contact
(irritant), Potential Chronic
Health Effects: The
substance is toxic to blood,
kidneys, lungs, liver, mucous
membranes, gastrointestinal
tract, upper respiratory
tract, skin, eyes, central
nervous system (CNS). The
substance may be toxic to
the reproductive system.
Closed system, ventilation,
explosion-proof electrical
equipment and lighting. Do
NOT use compressed air for
filling, discharging, or
handling
Ventilation. Remove all ignition sources.
Collect leaking liquid in sealable containers.
Absorb remaining liquid in dry sand or inert
absorbent and remove to safe place. Do NOT wash
away into sewer. Personal protection: complete
protective clothing including self contained
breathing apparatus
2 Bromine May be fatal if inhaled.
Highly toxic by inhalation,
ingestion or skin contact.
Causes severe burns.
Lachrymator. Typical TLV 0.1
ppm. Typical STEL 0.3 ppm.
The substance is toxic to
mucous membranes. The
substance may be toxic to
kidneys, liver, cardiovascular
system, central nervous
system (CNS), thyroid
Provide exhaust ventilation
or other engineering
controls to keep the
airborne concentrations of
vapors below their
respective threshold limit
value. Ensure that eyewash
stations and safety showers
are proximal to the work-
station location. Personal
Protection: Face shield. Full
suit. Vapor respirator. Be
sure to use an
approved/certified
respirator or equivalent.
Gloves. Boots.
Small Spill: Absorb with an inert material and put
the spilled material in an appropriate waste
disposal.
Large Spill: Corrosive liquid. Poisonous liquid. Stop
leak if without risk. Absorb with DRY earth, sand or
other non-combustible material. Do not get water
inside container. Do not touch spilled material.
Use water spray curtain to divert vapor drift. Use
water spray to reduce vapors. Prevent entry into
sewers, basements or confined areas; dyke if
needed. Call for assistance on disposal. Be careful
that the product is not present at a concentration
level above TLV.
3 Ethyl Alcohol The substance is toxic to
blood, the reproductive
system, liver, upper
respiratory tract, skin,
central nervous
Provide close process Flammable liquid. Keep away from heat. Keep
away from sources of ignition. Stop leak if without
risk. Absorb with DRY earth, sand or other non-
combustible material. Do not touch spilled
material. Prevent entry into sewers, basements or
confined areas; dyke if needed.
4 Dimethyl
formamide(DMF)
The substance is toxic to
kidneys, liver, central
nervous system (CNS). The
substance may be toxic to
blood, the nervous system.
Repeated or prolonged
exposure to the substance
can produce target organs
damage.
Provide exhaust ventilation
or
other engineering controls
to
Keep the airborne
concentrations of vapors
below their respective
threshold limit value.
Ensure that eyewash
stations and safety showers
are proximal to the work-
station location.
Flammable liquid. Keep away from heat. Keep
away from sources of ignition. Stop leak if without
risk. Absorb with DRY earth, sand or other non-
combustible material. Do not touch spilled
material. Prevent entry into sewers, basements or
confined areas; dyke if needed.
5 Hydrochloric
Acid
Very hazardous in case of
skin contact (corrosive,
irritant, permeator), of eye
contact (irritant, corrosive),
of ingestion, Slightly
Provide close process and
scrubber on process vent
and
storage vent
Corrosive liquid. Poisonous liquid. Stop leak if
without risk. Absorb with DRY earth, sand or other
non-combustible material. Do not get water inside
container. Do not touch spilled material. Use
water spray curtain to divert vapor drift.
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hazardous in case of
inhalation (lung sensitizer).
Non-corrosive for lungs.
Liquid or spray mist may
produce tissue damage
particularly on mucous
membranes of eyes, mouth
and respiratory tract. Skin
contact may produce burns.
Inhalation of the spray mist
may produce severe
irritation of respiratory tract,
characterized by coughing,
choking, or shortness of
breath. Severe over-
exposure can result in death.
6 Hexane The substance is toxic to
blood, the reproductive
system, liver, upper
respiratory tract, skin,
central nervous
Provide close process Flammable liquid. Keep away from heat. Keep
away from sources of ignition. Stop leak if without
risk. Absorb with DRY earth, sand or other non-
combustible material. Do not touch spilled
material. Prevent entry into sewers, basements or
confined areas; dyke if needed.
7 Isopropyl alcohol The substance is toxic to
blood, the reproductive
system, liver, upper
respiratory tract, skin,
central nervous
Provide close process Flammable liquid. Keep away from heat. Keep
away from sources of ignition. Stop leak if without
risk. Absorb with DRY earth, sand or other non-
combustible material. Do not touch spilled
material. Prevent entry into sewers, basements or
confined areas; dyke if needed.
8 Methanol The substance is toxic to
blood, the reproductive
system, liver, upper
respiratory tract, skin,
central nervous
Provide close process Flammable liquid. Keep away from heat. Keep
away from sources of ignition. Stop leak if without
risk. Absorb with DRY earth, sand or other non-
combustible material. Do not touch spilled
material. Prevent entry into sewers, basements or
confined areas; dyke if needed.
9 Liq. Ammonia Very hazardous in case of
skin contact (corrosive,
irritant, permeator),
Inhalation of the spray mist
may produce severe
irritation
of respiratory tract,
characterized by coughing,
choking, or shortness of
breath. Severe overexposure
can result in death. The
substance is toxic to upper
respiratory tract
Provide exhaust ventilation
or other engineering
controls to keep the
airborne concentrations of
vapors below their
respective threshold limit
value. Ensure that eyewash
stations and safety showers
are proximal to the work-
station location.
Dilute with water and mop up, or absorb with an
inert dry material and place in an appropriate
waste disposal container. If necessary: Neutralize
the residue with a dilute solution of acetic acid.
Corrosive liquid. Poisonous liquid. Stop leak if
without risk. Absorb with DRY earth, sand or other
non-combustible material.
Do not get water inside container. Do not touch
spilled material. Use water spray curtain to divert
vapor drift. Use water spray to reduce vapors.
Prevent entry into sewers, basements or confined
areas; dyke if needed. Call for assistance on
disposal. Neutralize the residue with a dilute
solution of acetic acid.
10 Methylene
Chloride
CARCINOGENIC EFFECTS:
Classified + (Proven.) by
OSHA. The substance is toxic
to lungs, the nervous
system, liver, mucous
membranes, central nervous
system (CNS).
Provide exhaust ventilation
or other engineering
controls to keep the
airborne concentrations of
vapors below their
respective threshold limit
value. Ensure that eyewash
stations and safety showers
Absorb with an inert material and put the spilled
material in an appropriate waste disposal. Be
careful that the product is not present at a
concentration level above TLV
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are proximal to the
workstation location.
Personal Protection:
11 Thionyl Chloride Corrosive. Extremely
destructive to tissues of the
mucous membranes and
upper respiratory tract.
Symptoms may include
burning sensation, coughing,
wheezing, and laryngitis,
shortness of breath,
headache, nausea and
vomiting. Inhalation may be
fatal as a result of spasm
inflammation and edema of
the larynx and bronchi,
chemical pneumonitis and
pulmonary edema.
Use process enclosure, local
exhaust ventilation, or
other engineering controls
to control airborne levels
below recommended
exposure limits. Facilities
storing or utilizing this
material should be
equipped with an eyewash
facility and a safety shower.
Use only under a chemical
fume hood.
Do not contact with water. Ventilate area of leak
or spill. Wear appropriate personal protective
equipment as specified in Section 8. Isolate hazard
area. Keep unnecessary and unprotected
personnel from entering. Contain and recover
liquid when possible. Neutralize with alkaline
material (soda ash, lime), then absorb with an
inert material (e. g., vermiculite, dry sand, earth),
and place in a chemical waste container. Do not
use combustible materials, such as saw dust. Do
not flush to sewer.
12 Toluene The substance is toxic to
blood, the reproductive
system, liver, upper
respiratory tract, skin,
central nervous
Provide close process Flammable liquid. Keep away from heat. Keep
away from sources of ignition. Stop leak if without
risk. Absorb with DRY earth, sand or other non-
combustible material. Do not touch spilled
material. Prevent entry into sewers, basements or
confined areas; dyke if needed.
13 Sulfuric Acid Prolonged or repeated skin
contact may cause
dermatitis. Prolonged or
repeated inhalation may
cause nosebleeds, nasal
congestion, erosion of the
teeth, perforation of the
nasal septum, chest pain and
bronchitis
Facilities storing or utilizing
this material should be
equipped with an eyewash
facility and a safety shower.
Use adequate general or
local exhaust ventilation to
keep airborne
concentrations below the
permissible exposure limits.
Use a corrosion-resistant
ventilation system.
Clean up spills immediately, observing precautions
in the Protective Equipment section. Carefully
scoop up and place into appropriate disposal
container. Provide ventilation. Do not get water
inside containers. Cover with dry earth, dry sand,
or other noncombustible material followed with
plastic sheet to minimize spreading and contact
with water.
14 EDC/ (1,2-
Dichloroethane)
The substance is toxic to
lungs, the nervous system,
liver, mucous membranes.
Repeated or prolonged
exposure to the substance
can produce target organs
damage. Repeated or
prolonged contact with
spray mist may produce
chronic eye irritation and
severe skin
Irritation. Repeated or
prolonged exposure to spray
mist may produce
respiratory tract irritation
leading to frequent attacks
of bronchial infection.
Provide exhaust ventilation
or other engineering
controls to keep the
airborne concentrations of
vapors below their
respective threshold limit
value. Ensure that eyewash
stations and safety showers
are proximal to the work-
station location.
Flammable liquid. Corrosive liquid. Keep away
from heat. Keep away from sources of ignition.
Stop leak if without risk. Absorb with DRY earth,
sand or other non-combustible material. Do not
get water inside container. Do not touch spilled
material. Use water spray curtain to divert vapor
drift. Prevent entry into sewers, basements or
confined areas; dyke if needed. Eliminate all
ignition sources. Call for assistance on disposal. Be
careful that the product is not present at a
concentration level above TLV.
15 Nitric acid The substance may be toxic
to lungs, mucous
membranes, upper
respiratory p. 2 tract, skin,
Provide exhaust ventilation
or other engineering
controls to keep the
airborne concentrations of
Corrosive liquid. Oxidizing material. Poisonous
liquid. Stop leak if without risk. Absorb with DRY
earth, sand or other noncombustible material. Do
not get water inside container. Avoid contact with
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eyes, and teeth. Repeated or
prolonged exposure to the
substance can produce
target organs damage.
Repeated or prolonged
contact with spray mist may
produce chronic eye
irritation and severe skin
irritation. Repeated or
prolonged exposure to spray
mist may produce
respiratory tract irritation
leading to frequent attacks
of bronchial infection.
vapors below their
respective threshold limit
value. Ensure that eyewash
stations and safety showers
are proximal to the work-
station location.
a combustible material (wood, paper, oil,
clothing...). Keep substances damp using water
spray. Do not touch spilled material. Use water
spray curtain to divert vapor drift. Use water spray
to reduce vapors. Prevent entry into sewers,
basements or confined areas; dyke if needed. Call
for assistance on disposal. Neutralize the residue
with a dilute solution of sodium carbonate. Be
careful that the product is not present at a
concentration level above TLV.
16 Xylene The substance is toxic to
blood, kidneys, the nervous
system, liver. Repeated or
prolonged exposure to the
substance can produce
target organs damage.
Provide exhaust ventilation
or other engineering
controls to keep the
airborne concentrations of
vapors below their
respective threshold limit
value. Ensure that eyewash
stations and safety showers
are proximal to the work-
station location.
Toxic flammable liquid, insoluble or very slightly
soluble in water. Keep away from heat. Keep away
from sources of ignition. Stop leak if without risk.
Absorb with DRY earth, sand or other non-
combustible material. Do not get water inside
container. Do not touch spilled material. Prevent
entry into sewers, basements or confined areas;
dyke if needed. Eliminate all ignition sources. Call
for assistance on disposal. Be careful that the
product is not present at a concentration level
above TLV.
17 Phenol The substance may be toxic
to kidneys, liver, central
nervous system (CNS).
Repeated or prolonged
exposure to the substance
can produce target organs
damage. Repeated p. 2
exposure of the eyes to a
low level of dust can
produce eye irritation.
Repeated skin exposure can
produce local skin
destruction, or dermatitis.
Repeated inhalation of dust
can produce varying degree
of respiratory irritation or
lung damage. Repeated
exposure to a highly toxic
material may produce
general deterioration of
health by an accumulation in
one or many human organs.
Use process enclosures,
local exhaust ventilation, or
other engineering controls
to keep airborne levels
below recommended
exposure limits. If user
operations generate dust,
fume or mist, use
ventilation to keep
exposure to airborne
contaminants below the
exposure limit.
Corrosive solid. Stop leak if without risk. Do not
get water inside container. Do not touch spilled
material. Use water spray to reduce vapors.
Prevent entry into sewers, basements or confined
areas; dyke if needed. Eliminate all ignition
sources. Call for assistance on disposal. Be careful
that the product is not present at a concentration
level above TLV.
18 Chlorine Toxic by inhalation. Irritating
to eyes, respiratory system
and skin. Very toxic to
aquatic organisms.
Use only with adequate
ventilation. Use process
enclosures, local exhaust
ventilation or other
engineering controls to
keep worker exposure to
airborne contaminants
below any recommended or
statutory limits.
Immediately contact emergency personnel. Keep
unnecessary personnel away. Use suitable
protective equipment. Eliminate all ignition
sources if safe to do so. Do not touch or walk
through spilled material. Shut off gas supply if this
can be done safely. Isolate area until gas has
dispersed.
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6.6.1.10 TRAINING AND EDUCATION OF EMPLOYEES AND PERSONAL PROTECTIVE
EQUIPMENTS
Safety awareness training programmes are arranged regularly through safety department
and safety-training programmes are also arranged for workers & staff working in the factory
premises. External faculties are also invited the lectures on the matter of safety in a
practical manner understandable to the workers & staff.
M/s. Paushak Ltd. gives training on the following subjects;
Accident Prevention Technique
Basic fire fighting
Use of Respiration PPE
Handling of Hazardous chemicals
Use of chlorine kit
First Aid program
Breathing Apparatus practical Programme
General safety regulation
Permit to work system
Electrical safety
HAZOP study
On site emergency plan training
MSDS Awareness
SHE SOP’s
Once in a month workmen for different plant are grouped together & practical classes are
held to train them how to operate various types of fire extinguisher to wear the mask, SCBA
apparatus, use of cylinder handling kits. Usefulness of each part of the chlorine kits is also
explained. Fire dill is also conducted regularly. Personal protective equipment such as safety
shoes, safety goggles, hand gloves, gum boots, safety helmet have been given to each
workers & staff. Provided seven nos. of SCBA set with standby extra cylinders in entire
premises, Airline mask provided in each plant. All type of PPE are kept in all related area, we
check them regularly. Fire hydrant points & eye wash showers have been installed at various
places and at various floors of the plant building. They have been instructed how to use.
Maintaining plant as per GFR guidelines.
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6.6.1.11 MEDICAL SURVEILLANCE PROGRAM
Pre-employment Medical Check Up
1. Chest X-ray
2. Cardiogram
3. Audiometry
4. Hematological Examination:- CBC, SGOT, SGPT, Cholesterol, Blood Sugar etc
5. Urine Examination
6. Vision test
7. Colour blindness test
8. Lung function test- Spirometry
Periodical Medical Check up
1. Lung Function test
2. Cardiogram
3. Audiometry
4. Hematological Examination
5. Urine examination
6. Vision test
7. Colour blindness test
8. Biomarker in Blood & Urine
6.6.2 SAFETY PLAN
Safety of both men and materials during construction and operation phases is of concern.
Safety plan shall be prepared and implemented in the proposed project activity. The
preparedness of an industry for the occurrence of possible disasters is known as emergency
plan. The disaster in the plant is possible due to collapse of structures and fire/explosion etc.
The proposed expansion project would formulate safety policy keeping in view the
safety requirement during construction, operation, maintenance phases, with the
following regulations:
To allocate sufficient resources to maintain safe and healthy conditions of work;
To take steps to ensure that all known safety factors are taken into account in the
design, construction, operation and maintenance of plants, machinery and
equipment;
To ensure that adequate safety instructions are given to all employees;
To provide wherever necessary protective equipment, safety appliances and clothing
and to ensure their proper use;
To inform employees about materials, equipment or processes used in their work
which are known to be potentially hazardous to health or safety;
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To keep all operations and methods of work under regular review for making
necessary changes from the point of view of safety in the light of experience and up
to date knowledge;
To provide appropriate facilities for first aid and prompt treatment of injuries and
illness at work;
To provide appropriate instruction, training, retraining and supervision to employees
in health and safety, first aid and to ensure that adequate publicity is given to these
matters;
To ensure proper implementation of fire prevention methods and an appropriate fire
fighting service together with training facilities for personnel involved in this service;
To organize collection, analysis and presentation of data on accident, sickness and
incident involving people injury or injury to health with a view to taking corrective,
remedial and preventive action;
To promote through the established machinery, joint consultation in health and
safety matters to ensure effective participation by all employees;
To publish/notify regulations, instructions and notices in the common language of
employees;
To prepare separate safety rules for each type of occupation/processes involved in a
plant; and
To ensure regular safety inspection by a competent person at suitable intervals of all
buildings, equipments, work places and operations.
6.6.3 SAFETY ORGANIZATION
Construction and Erection Phase
A qualified and experienced safety officer shall be appointed. The responsibilities of the
safety officer include identification of the hazardous conditions and unsafe acts of workers
and advice on corrective actions, conduct safety audit, organize training programs and
provide professional expert advice on various issues related to occupational safety and
health. He is also responsible to ensure compliance of Safety Rules/ Statutory Provisions.
Operation and Maintenance Phase
When the construction is completed the posting of safety officers shall be in accordance
with the requirement of Factories Act and their duties and responsibilities shall be as
defined there of.
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6.6.4 SAFETY CIRCLE
In order to fully develop the capabilities of the employees in identification of hazardous
processes and improving safety and health, safety circles would be constituted in each area
of work. The circle would consist of about five to six employees from that area. The circle
normally shall meet for about an hour every week.
6.6.5 SAFETY TRAINING
Safety training shall be provided by the Safety Officers with the assistance of faculty
members called from Professional Safety Institutions and Universities. In addition to regular
employees, limited contractor labors shall also be provided safety training. To create safety
awareness safety films shall be shown to workers and leaflets shall be distributed.
Some precautions and remedial measures proposed to be adopted to prevent fires are:
Compartmentalization of cable galleries, use of proper sealing techniques of cable
passages and crevices in all directions would help in localizing and identifying the
area of occurrence of fire as well as ensure effective automatic and manual fire
fighting operations;
Spread of fire in horizontal direction would be checked by providing fire stops for
cable shafts;
Reliable and dependable type of fire detection system with proper zoning and
interlocks for alarms are effective protection methods for conveyor galleries;
Housekeeping of high standard helps in eliminating the causes of fire and regular fire
watching system strengthens fire prevention and fire fighting; and
Proper fire watching by all concerned would be ensured.
6.6.6 HEALTH AND SAFETY MONITORING PLAN
The health of all employees shall be periodically monitored for early detection of any
ailment due to exposure to heat and noise.
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6.7 TRAINING, REHERASAL & RECORDS
6.7.1 NEED OF TRAINNING & REHEARASAL
Training is important in order to –
Teach worker’s how to handle chemicals safely, how to act as a runner/messenger, how
to use PPE, how to start and shut down the plant, how to carry out emergency repairs
etc.
Teach one to be a safe and alert worker.
Rehearsal is essential for -
Explaining and making key personnel and essential workers aware of their role in
case of an emergency.
Testing the emergency procedure, emergency arrangements and ability of all
involved with it to grasp the procedure and implement the same.
Testing the effectiveness of communication system including the alternative
arrangement in case of failure.
Testing the speed of mobilization of resources, search, rescue and treatment of
casualties, emergency isolation and shut down.
Detecting the shortcomings in the emergency plan and incorporating remedial
measures.
Allowing professional emergency services to test their parts of the plan and testing
co-ordination.
Building confidence in workers which is helpful in facing real situations.
Training shall be given to regular employees and contract personnel also. Effective and
latest teaching aids will be used to train workers and supervisory staff. Such training courses
shall be conducted once in a year and co-ordination with offsite personnel shall be sought
during such training. Records will be maintained for training.
6.7.2 SOME CHECK POINTS
Following points can be checked at the time of training/assessing the adequacy of the
Emergency Plan.
Does the plan cover the range of incidents that can realistically be anticipated?
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Have the consequences of the various incidents considered been adequately assessed?
Are there sufficient resources in terms of personnel and equipment on the site to carry
out the Emergency Plan for the various incidents in conjunction with the public
emergency services?
Have the time scales been assesses correctly?
Is there a logical sequence of actions for each person given a role in the plan? Whether
key personnel, especially the nominated incident controllers, consulted in the
preparation of the plan?
Is there 24 hours cover, to take account of absences due to sickness and holidays,
minimum shift manning, operator only periods, silent hours, shutdown periods, only
security personnel being present, or for unmanned sites etc.?
Is there satisfactory co-operation with the local emergency services and district
emergency planning officers?
At sites where an off-site plan to protect people and the environment outside the site in
the event of an incident is appropriate what is the procedure for initiating the off-site
plan and is this satisfactory?
6.7.3 RECORDS AND UPDATING THE PLAN
All records of On-Site and Off-Site Emergency Plan and modifications by experience and
suggestion, the rehearsals and conclusions of such plans and the enquiries shall be well
maintained and preserved. The necessary data bank shall be also maintained for the utility
of industries and others. New information and the deficiencies identified during the
rehearsal is reviewed and incorporated in the document for continual up dating of the plan
and such information shall be communicated to the concerned authorities.
6.8 HAZOP STUDY
6.8.1 OBJECTIVE
For identifying cause and the consequences of perceived mal operations of equipment and
associated operator interfaces in the context of the complete system. It accommodates the
status of recognized design standards and codes of practice but rightly questions the
relevance of these in specific circumstances where hazards may remain undetected.
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6.8.2 PURPOSE OF HAZOP
It emphasizes upon the operating integrity of a system, thereby leading methodically to
most potential and detectable deviations which could conceivably arise in the course of
normal operating routine
- including "start-up” and "shut-down" procedures
- as well as steady-state operations.
It is important to remember at all times that HAZOP is an identifying technique and not
intended as a means of solving problems nor is the method intended to be used solely as an
undisciplined means of searching for hazardous scenarios.
6.8.3 FEATURES OF HAZOP STUDY
Subsystems of interest line and valve, etc
Equipment, Vessels
Modes of operation Normal operation
Start -up mode
Shutdown mode
Maintenance /construction / inspection mode
Trigger events Human failure
Equipment /instrument/component failure
Supply failure
Emergency environment event
Other causes of abnormal operation, including
instrument disturbance
Effects within plant Changes in chemical conditions
Changes in inventory
Change in chemical physical conditions
Hazardous conditions Release of material
Changes in material hazard characteristics
Operating limit reached
Energy source exposed etc.
Corrective actions Change of process design
Change of operating limits
Change of system reliability
Improvement of material containment
Change control system
Add/remove materials
How would hazardous During normal operation
Conditions detected? Upon human failure
Upon component failure
In other circumstances
Contingency actions Improve isolation
Improve protection
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6.8.4 HAZOP STUDY PROCEDURE
• Procedure in HAZOP study consists of examining the process and instrumentation (P&I)
line diagram, process line by process line.
• A list of guide words is used to generate deviations from normal operation
corresponding to all conceivable possibilities.
• Guide words covering every parameter relevant to the system under review i.e. flow
rate and quality, pressure, temperature, viscosity, components etc.
• Flowchart for application of HAZOP is shown in figure.
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HAZOP STUDY FLOW CHART
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GUIDE WORDS
NONE No forward flow when there should be
MORE More of any parameter than there should be, e.g. more
flow, more pressure, more temperature, etc.
LESS As above, but "less of" in each instance
PART System composition difference from what it should be
MORE THAN More "components" present than there should be for
example, extra phase, impurities
OTHER What needs to happen other than normal operation, e.g.
start up, shutdown, maintenance?
NONE e.g., NO FLOW caused by blockage; pump failure; valve
closed or jammed: leak: valve open; suction vessel empty;
delivery side over - pressurized: vapor lock; control failure
REVERSE e.g., REVERSE FLOW caused by pump failure: NRV failure or
wrongly inserted; wrong routing; delivery over pressured;
back- siphoning; pump reversed
MORE OF e.g., MORE FLOW caused by reduced delivery head ; surging
; suction pressurized ; controller failure ; valve stuck open
leak ; incorrect instrument reading.
MORE OF MORE TEMPERATURE, pressure caused by external fires;
blockage ; shot spots; loss of control ; foaming; gas release;
reaction; explosion; valve closed; loss of level in heater; sun.
LESS OF e.g., LESS FLOW caused by pump failure; leak; scale in
delivery; partial blockage ; sediments ; poor suction head;
process turndown.
LESS e.g., low temperature, pressure caused by Heat loss;
vaporization; ambient conditions; rain; imbalance of input
and output; sealing; blocked vent.
PART OF Change in composition high or low concentration of mixture;
additional reactions in reactor or other location; feed
change.
MORE THAN Impurities or extra phase Ingress of contaminants such as
air, water, lube oils; corrosion products; presence of other
process materials due to internal leakage ; failure of
isolation ; start-up features.
OTHER Activities other than normal operation start-up and
shutdown of plant ; testing and inspection ; sampling ;
maintenance; activating catalyst; removing blockage or scale
; corrosion; process emergency ; safety procedures activated
; failure of power, fuel, steam , air, water or inert gas;
emissions and lack of compatibility with other emission and
effluents.
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6.8.5 PROCESS HAZARD AND ITS CONTROL
In charge Person
Sr.
No.
Name of the
Plant,
Department and
Operation.
Name of
hazardous
process and
operation.
Materials in the
process /
Operation with
their quantity.
Name of the
vessel and its
location.
Operating
parameters :
pressure,
temperature
etc.
Type of hazards
possible
(exothermic, run
away, pressure
release, fire,
explosion etc.)
Control measure provided Name &
Designation
Telephone
number
1 2 3 4 5 6 7 8 9 10
1 GTF Plant D14 reaction
SPD
RVD
EDA -2.4 mt
CS2- 7 mt
12 mt height
Storage tank 1
900 mmwc
Temp 40to
428c
sPD 290*c
Pressure
Fire in SPD
PLC control
As per temp limit
operation stop
new new
2
GTI plant Isomerization
Acetylation
ANF
SFD
DMPAT 7 mt
AC20 4.5 mt
Ethyl acetate -15
mt
12 mt height
18 mt
24 mt
Storage tank 2
50to 55*C
kg/cm2
100*c steam
temp
RUN away
Fire in SFD
PLC control
As per temp limit
operation stop
new new
3 Intermediate
plant
PCL3 rxn
PScl3 rxn
Monoester
Di ester
Pcl3 -50 mt
Sulpher-20 mt
Methanol-30 mtl
Liq amm -20 mt
6 mt height
12 mt height
18 mt
24 mt
Storage tank 4
115 *C
10 to 15*c
Highly
exothermic
& explosionn
PLC control
As per temp limit
operation stop
new new
4 GTH plant Hydrogenation
Nitration
Chemical &
thermal
denitratuioin
Hydrogenation
mass =34 mt
Nitration
mass=30 mt
Chemical de
nitration mass=5
mt
Acetone
Heptane
EDC
Auto calve
Nitration
Chemical
denitartion
Thermal de
nitration
Dissolution
purification
95 to 100*c Safety valve
Temp controller
At
Hydrogenation&
nitration stage
PLC control
As per temp limit
operation stop
Hydrogen sensor
new new
5 Chlorine &
hydrogen
handling
Cl2 tank farm
Hydrogen trolley
Cl2 tank farm 10
mt
Hydrogen trolley-
1200 m3
Ground level RT Scrubbing system Cl2 & Hydrogen sensor new new
5 Tank farm &
material handling
Tanker unloading
C2s =100 mt
EDA =200 mt
Mnso4 =500 mt
Znso4=100 mt
Clye=200 mt
Ground level RT Over flow
Static generation
Leakages from
piping /Valve
Smell from Vent
Earthing
Safety valve
Thickness
Dyke valve
Check list
Flame arrestor /breather
valve
Scrubber
sensor
new new
3 Process control &
equipment safety
system
Over pressure
High Temp
Instrument
failure
PLC failure
On equipment
& plant
RT Explosion
Fire
Human error
Safety valve /RD/BPRV
inspection
Instrument calibration
PLC healthy
New new
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6.8.6 PLANNING FOR HAZOP
• Safety procedures documents
• Relief/venting philosophy
• Chemical involved
• Piping specifications
• Carry out the study
• Record the results
• Follow-up of actions noted
1. Final report contains resolution of all recommended actions.
2. Must appoint someone as leader to check progress of action.
3. Team may meet again if answers to questions do not simply lead to an action.
4. Team may meet again if significant design changes in interim report.