mock drill oil bottling plant ban gal ores

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    Mock Exercise on Chemical(Industrial Disaster)

    Indian Oil Corporation Ltd.

    LPG Bottling Plant, Devanagunthi

    Vijay Kumar C.

    Sr. Plant Manager

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    Profile of Devanagunthi LPG Bottling Plant

    Plant is situated at Devanagunthi.

    45 Km from Banglore Dist HQ.

    Neighbouring Industries

    1. IOCL (Terminal) 1.0 Km away2. BPCL (Terminal) 1.25 Km away

    3. HPCL (Installation)- 1.5 Km away

    4. Petronet MHB Limited-1.25 Km away

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    Indane bottling plantLayout

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    Major Activities

    LPG receipt by rail and road,Storage, bottling & Despatch

    Loading of LPG bullet trucks forAuto LPG Dispensing stations andother bottling plants

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    Bulk LPG Receipt

    Source of Receipt : Rail Wagons fromMangalore and

    Hazira and road tankersfrom CPCL

    Supply Area : Bangalore city,Peripheral marketsof Bangalore city

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    LPG BOTTLING PLANT, DEVANAGUNTHI MAH INDUSTRY

    Bottling Capacity

    Existing : 138 TMTPA

    Proposed: 232 TMTPA

    Total Land Area : 93.35 ACRES

    Green belt Area : 25 ACRES

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    Bulk LPG Storage Facilities

    Sphere 2 x 1400 MT

    Bullets 2 x 100 MT

    Bullet 1 x 150 MT

    Additional Mounded 3 x 1200 MT

    Bullets

    Existing 3150 MT After Augumentation

    6750MT

    Existing

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    By Road

    12 nos. Tank lorry unloading bayswith unloading arms.

    By Rail

    Two spur full rake gantry unloadingfacility. Equipped to unload both

    conventional and BTPGLN wagons.

    Bulk Receipt Facilities

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    Population in nearby VillagesSl. No. Name of the village Population

    1 Kacharakanahalli 437

    2 Dasarahalli 4583 Geddlapura 163

    4 Dodda Donnasandra 1677

    5 Kannekal 410

    6 Makkanahalli 1465

    7 Devalapura 446

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    Material Safety DataIDENTITY OF MATERIAL :

    Product Name LPG. Bottle gas,Liquefied

    hydrocarbon gas.

    UN No. 1075

    Label / Class Red: Flammable

    Liquid / 2.1Trade name LPG

    Formula Mixture of

    propane and

    butane

    HAZCHEM Code 2WE

    PHYSICAL AND CHEMICAL PROPERTIES

    Physical State Gas Boiling Point / Range , deg.

    C

    1 Vapor Pressure

    at 65 deg. C,

    16.9 kg/cm2

    Appearance Colourless Melting / Freezing Point ,

    deg. C

    138

    Odor Odorless/stanche

    d

    Vapor Density (Air =1) 1.5 to 2.0

    Solubility in Water Insoluble Specific Gravity , 20 deg. C 0.53 to 0.57

    Calorific Value

    (Kcal / Kg.)11400 Dyn. Viscosity (PA.S 30

    deg. C)

    Molecular Weight.

    FIRE AND EXPLOSIVE DATA

    Explosivity Highly explosive Auto Ignition Temp. deg. C 405-450

    Flammability Dangerous Explosive Limits , % 1.8 9.6

    Extinguishing Media CO2, DCP. Water spray may be used to control and confine LPG fires.

    Special Procedures Do not attempt o extinguish fire until leak has been shut off. For small fire use dry chemicals. Let large fires burn if not heating

    the container. When exposed to heat and flame, containers may rupture due to BLEVE

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    Risk Analysis

    Based on three steps

    What can go wrong?

    (Hazard identification)

    How often it can go wrong?

    (Failure frequency)

    What are the effects of consequences?

    (Effect and damage calculations)

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    MODES OF FAILURE OF

    PRODUCT STORAGE VESSELS

    Material and construction failures

    Corrosion

    Gasket failures

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    PRINCIPAL HAZARDS - LPG

    Flammability & Explosion

    Jet Fire

    Pool Fire

    BLEVE

    Flash Fire

    UVCE

    Asphyxia

    Cold Burns

    Metal brittleness due to Low temperature

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    Consequences Analysis

    Damages are caused due to

    Heat radiation

    Overpressure effect from explosions

    Toxic effect

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    Exposure time, heat radiation anddamage levels

    Intensity of

    radiation (Kw/

    m2

    Exposure

    time in

    Seconds

    % Lethality

    37.5 28 100% Lethality

    12.5 28 1% Lethality /100 % first deg.burns4 28 1% first degree burns

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    Damage distance for BLEVE

    37.5 KW/m2 12.5 Kw/m2 4.0 KW/m2

    HORTONSPHERE

    1400 273 524 908 1830

    Storage

    Vessel

    LPG in

    MT

    BLEVE

    Radious(m)

    Radiation distance in meters to

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    Damage contour for catastrophic failure of 1400 MT sphere

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    Zone AZone A 37.5 Kw/M2 524

    M rad 100% lethality

    (Plant personnel)

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    Zone B

    12.5 Kw/M2 908 M rad 1% lethal

    (Kanekkal Village)

    Zone - B

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    Zone C

    - 4.0 Kw/M2

    - 1830 M

    - First Degree burns(Kacharakanahalli, Dasarahalli,

    Giddapura,Doddasandra)

    Zone C

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    Risk intensity

    ZoneRadiation

    (KW/M2)

    Distance in

    meter

    Zone A 37.5 524 Plant Personnel 80

    Zone B 12.5 908 Kanekal village 443

    Kacharaknahalli 472

    Dasarahalli 495

    Gidlapura 176

    Donnasandra 1811

    Makanahalli 1582

    Devalapura 482

    Vagatta 1103

    Neighboring

    industries400

    Affected population

    Zone C 4 1830

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    Gas Monitoring System

    Air/Vapor Extraction System

    Remote control Valve

    Emergency Trip Button

    Manual Call point

    Quartzoid bulb detector.

    Mitigation measures

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    FIRE WATERSTORAGE TANKS

    3 Nos. of 4000 KL capacity each

    FIRE PUMPS

    8 Nos. diesel driven waterpumps of 410 CUM/ Hr. capacity each.

    JOCKY PUMPS

    2 Nos. of 24 Cum /Hr.

    Fire Fighting Facilities

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    Ring main hydrant system

    57 double hydrant points

    46 water monitors 4 long range monitors coveringtruck Parking Area.

    Auto sprinkler system forSheds

    , TLD , Storage Vessels andTank Wagon Gantry.

    Fire Fighting Facilities

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    Carousel Inter locked with Vapour extractionsystem

    Remote operated valves for LPG pipe lineinter locked with sprinkler system

    LPG and Air compressors inter locked withcooling waterpumps.

    Emergency trip buttons and Manual callstations at strategic points.

    ROV closure ofStorage Vessel interlockedwith HLAs.

    Additional Safety Features

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    Detailed on-site emergencymanagementplanprepared andapproval obtained from Dept. ofFactories.

    Emergency Response Drills(ERDs) are conducted twice in ayear.

    Mock drills are conducted

    every month & shortcomings areaddressed.

    Mutual aid arrangement withneighbouring industries.

    On-site Emergency Plan

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    Mutual Aid

    To Assist its neighbouring industries in responding to

    emergencies that may occur either on-site or off-sites.

    Member Roles and responsibilities

    IOCL, Terminal Traffic control and smooth evacuation of trucks

    BPC Terminal Assist the Rescue Team membersHPCL Installation Assist Auxilliary team members

    PETRONET Assist Auxilliary team members

    Mutual Aid agreemnt

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    Fire Fighting Organisation Chart

    FIRE COMBAT TEAM AUXILIARY TEAM RESCUE TEAM

    Team In Charge: Floor Officer Team In Charge:

    Manager (P)

    Team In Charge: Asst.

    Manager (F)

    Alternate team Incharge: Officer

    (Bulk Operations)

    Alternate team Incharge: S&D

    officer

    Alternate team Incharge:

    Accounts officer-II

    Assisted by: Assisted by: Assisted by:

    1. Tally operator 1 1. Dy. Manager (P) 1. A O - II2. Tally operator 2 2. Safety Officer 2. Sr. Assistant3. Segregation 1 3. Maintenance Officer4. Segregation 2 4. Maintenance operator 15. Pump House 1 5. Maintenance operator 26. TLD 6. Employees on Relief

    7. Carousel Tare wt. 1 7. Security guard 3(Stores)

    8.Carousel Tare wt. 2 8. Security guard 4

    9. Evacuation (Gate 2)10. ICU11. Gantry operator 112. Gantry operator 213. Security guard 1(Main gate)

    14. Security guard 2 (Maingate)

    15. Security guard 3(Patrolling)

    FIRE IN CHIEF: Sr. Plant ManagerAlternate FIRE IN CHIEF: Manager (P)

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    Emergency Transport facility

    Dedicated Vehicle for emergency

    transportation is available round the clock.

    Between 08.00 hr to 17.15 hr one more

    vehicle also will be available.

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    Shutting down procedure

    Shutting down is done through the following

    means:

    Emergency trip Buttons & Manual Call

    Point

    Remote Control Valves

    Quartzoid Bulb detector.

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    On site Emergency Structure

    The basic concep

    t of thisp

    lan is top

    rovide a comp

    rehensiveapproach for managing emergencies. Four elements of this

    plan are

    Prevention - incorporates all those activities that eleminate

    theprobabilityof disaster occuring on-site.

    Preparedness - includes all activities necessary to ensure

    a high degree of readiness

    Response- measures taken during an incident which

    minimise damage to life and property.

    Recovery includes those short and long-term activitiesthat return all systems to normal operations.

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    Declaration of Emergency

    Upon declaration of Emergency Sr.Plant Manager

    makes initial assessment of incident and determine the need for

    evacuation.

    ensure that all personnel are accounted for.

    ensure that outside agencies are communicated as per DMP asfollows:

    Dy. Commisioner

    Regional, State & Head Offices

    Fire Dept

    Law & Order

    Revenue Dept

    Local Panchayat

    Railways

    KPTCL

    Medical Dept.

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    Public Awareness Programs

    Various programs being conductedFor creating public awareness to the

    Neighboring villages.

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