boiler water chemistry
DESCRIPTION
Water ChemistryTRANSCRIPT
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Boiler Water Management
Water Characteristics and Quality
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Fundamental Mission of BoilerPower House Management
Reliable production of steam• continuous & quality steam (no unplanned outages)
Safe production of steam• no injuries. no loss of capital equipment• Food safety: FDA. Kosher
Protect the capital investment• minimize corrosion and scaling
Environmental/Regulatory ComplianceCost effective operation• efficient as possible
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Water characteristics and qualityCharacteristics
pH important parameter (acidity. alkalinity)
Hardness combination of Ca and Mg
Conductivity uS/cm (relationship with dissolved solids)
Total Dissolved Solids amount of dissolved ions (mg/l)
Alkalinity amount of buffering
p-alkalinity titration until pH=8.3
m-alkalinity total alkalinity (pH=4.3)
Total Suspended Solids everything that is not dissolved and can be filtered out
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Water characteristics and qualityImpurities
MINERALS AIR EARTH
CationsAnions
OxygenCarbon MonoxideCarbon Dioxide
ClaySiltSand
a. Dissolved solids b. Dissolved gases c. Suspended matter
Anions
Bicarbonate HCO3-
Chloride Cl-
Sulphate SO42-
Nitrate NO3-
Silicate HSiO3-
Cations
Sodium Na+
Potassium K+
Calcium Ca2+
Magnesium Mg2+
Ammonium NH4+
Iron Fe2+
Manganese Mn2+
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Water characteristics and qualitypH Scale
ACIDIC BASIC
Hydrogen Ions (H+) decrease pH; Hydroxyl (OH-) increase pH
1 2 4 5 6 7 8 9 10 11 12 13 143
pH
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Water Characteristics and qualityThree battles
Presence of troublesome water components requires• Deposition Control
– Preventing overheat failures resulting from waterside deposition
• Corrosion Control– Maintaining materials of construction. dealing with
general and localized corrosion mechanisms• Steam Purity
– Preventing carryover of boiler water salts into steam phase
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Deposition
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DepositionWhat is
• Result of insolubility of inorganic scale formers– Hardness Based Deposits – Metal Oxide Based Deposits
• Can occur as a result of contaminated condensate or feedwater components
– Unlikely with demineralized makeup water– Good pretreatment may limit deposition potential
• Develops at areas of highest heat input• Issue becomes more critical as boiler pressure goes up
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Deposition Problems caused
Loss of Boiler Efficiency• Scale reduces heat transfer• Increased fuel/energy consumption
Boiler Tube Failure• Scale elevates tube temperature - causing tube
overheating• Partial destroyed boiler sections and even boiler
explosion due to overheating of tube metal over critical temperature for steel
Under-deposit Corrosion• Caused by high localized concentration of corrosive
molecules
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DepositionEfficiency reduction
Water tube boiler, 95 % of Scale CaCO3. No heat recovery20 bar [290 psi], 11.3 ton/h
Deposit in mm
0
2
4
6
8
10
12
14
16
18
20
0
0.4
0.8
1.2
1.6 2
2.4
2.8
3.2
3.6 4
4.4
4.8
Effi
cie
ncy L
oss in
%
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DepositionIncreased tube temperature
BScaled surface
resulting in lower T0
while needed T1
Deposit
Wal T2
Resulting boilerwater T0
Boiler water T1
needed
Boiler tubemetal wall
Wall T2
AClean internal heat transfer surface.
T1 for neededsteam production
Boiler tubemetal wall
Boiler water T1
Increasedwall T4
T3
Boiler water T1
CScaled surface
Fire side T2 is increasedto T4 to reach water T1
T3 is critical for metal structure
DepositBoiler tubemetal wall
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DepositionEffect of scale on heat transfer
0
40
80
120
160
200
240
0 0.002 0.004 0.006 0.008 0.01
Deposit thickness [mm]
Tem
pera
ture
[°F
]
Ana
lcite
(sod
ium
alu
min
um s
ilica
te)
Magnesium p
hosphate
Magnetic iron oxide
Calcium phosphate
115
95
70
50
25
5
Tem
pera
ture
[°C]
120
100
80
60
40
20
0
Tu
be m
eta
l te
mp
era
ture
in
cre
ase
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DepositionFactors
Factors that contribute in waterside deposition:• Presence of ionic scale formers in feedwater (calcium,
magnesium, barium, strontium, silica, iron)• Presence of scale formers treatment derived
(phosphate, alkalinity)• Presence of particulate contaminants• Interactions with existing deposition• Heat input• Flow parameters• “Microclimates” • Location in riser circuit
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DepositionSolubilities
Compound ppm as CaCO3
0 °C [32 °F] 100 °C [212 °F]
Calcium Bicarbonate 1620 Decomposes
Carbonate 15 13
Sulfate 1290 1250
Magnesium Bicarbonate 37.000 Decomposes
Carbonate 101 75
Sulfate 170.000 356.000
Sodium Bicarbonate 30.700 Decomposes
Carbonate 61.400 290.000
Chloride 225.000 243.000
Hydroxide 370.000 970.000
Sulfate 33.600 210.000
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DepositionHardness precipitation
• Precipitation of insoluble hardness
– 2 HCO3- CO3
2- + CO2+ H2O 100%
– CO32- + H2O CO2 + 2OH- 60 -
80%
– Ca2+ + CO32- CaCO3 boiler scale
– Mg+2 + OH- MgOH+
– H2SiO3 H+ + HSiO3-
– MgOH+ + HSiO3- MgSiO3 + H2O
• Exceeding saturation through evaporation, resulting in crystallization
– eg. CaSO4.SiO2
Scaling & DepositsHeat transfer limitation
Boiler tube failure
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DepositionWhy Hardness is Such an Issue
Temperature
Soluble Amount
Most materials are more soluble
at increasing temperature
Ca. Mg. Ba. Sr solubility decreases at increasing
temperature
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DepositionBoiler deposits
Name Formula
Acmite Na2O·Fe2O3·4SiO2
Analcite Na2O·Al2O3·4SiO2·2H2O
Anhydrite CaSO4
Aragonite CaCO3 (gamma form)
Basic magnesium phosphate Mg3(PO4)2·Mg(OH)2
Brucite Mg(OH)2
Calcium hydroxide Ca(OH)2
Calcite CaCO3 (beta form)
Copper Cu
Cuprite Cu2O
Ferrous oxide FeO
Goetnite Fe2O3 · H2O (alpha form)
Gypsum CaSO4·2 H2O
Hematite Fe2O3
Hydroxyapatite Ca10(PO4)6(OH)2
Magnetite Fe3O4
Serpentine (magnesium silicate) 3MgO·SiO2·2 H2O
Sodium ferrous phosphate NaFePO4
Tenorite CuO
Thenardite Na2SO4
Xonotlite 5 CaO·5 SiO2 ·H2O
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DepositionSilica
• Forms deposits in boilers • Occurs as magnesium silicate or silicic acid
• Selective silica carryover– Silica is selectively dissolved into the steam– Controlled by limiting the silica concentration in the
boiler water– Controlled by limiting boiler pressure– Controlled by maintaining high pH– Cannot be controlled mechanically by steam
separators• Not usually a problem with boilers with less than 40
bar (600 psig) pressure
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Deposition Iron scale
Iron is usually found in a boiler as one or more of the following:• A complex with calcium• A complex with phosphate• Hematite - Fe2O3• Magnetite - Fe3O4
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Corrosion
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CorrosionWhat is
Definition• The deterioration of a material by the interaction with
it’s environment
Impact• Feedwater piping• Feedwater heaters• Economizer• Boiler• Condensate system• …
Oxygen corrosion in flame pipe (6 bar boiler)
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CorrosionProblems caused
Impact corrosion on boiler reliability• Premature replacement need of boiler
– boilers should last very long upon correct use– Water side corrosion should be nihil and not a factor
contributing to the life time of the boiler• Unscheduled maintenance to boiler or feed water lines• Unscheduled maintenance to the condensate system• Filthy steam and condensate traps can cause leaking
of steam into condensate system due to malfunctioning valves
Oxygen corrosion in flame pipe (6 bar boiler)
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CorrosionBoiler metal passivation
Natural passivation:• Formation of a protective barrier on metal surface by
reaction with waterFe + 2 H2O Fe(OH)2 + H23Fe(OH)2 Fe3O4 + H2 + 2H2O
• Black magnetite film - Fe3O4• Rate of Magnetite formation is
– Temperature dependent– Spontaneous above 180 °C (360 °F)
• Reduces general corrosion• Difficult to quantify results
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Oxygen scavengingMetal passivation
SHIKORR REACTION
T < 180 °C• 3 Fe + 6 H2O 3 Fe(OH)2 + 3 H2
• 2 Fe(OH)2 + 2 H2O 2 Fe(OH)3 + H2
• Fe(OH)2 + 2 Fe(OH)3 Fe3O4 + 4 H2O
T > 180 °C• 3 Fe + 4 H2O Fe3O4 + 4 H2
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CorrosionSolubility of magnetite in water
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CorrosionEffect of pH
Do we have a better
picture ??
Check advanced training series
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CorrosionTypes
Types of Corrosion• Oxygen corrosion• Alkalinity concentration• Caustic corrosion• Acid corrosion• Chelant corrosion• Erosion/Corrosion
Condensate return pipe with deep attack due to the combined effect of CO2 and O2
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CorrosionOxygen Corrosion
ANODE: Fe0 Fe+2 + 2e-
Natural Metal Metal ion Metal electrons
CATHODE: 2e- + 1/2 O2 + H2O 2(OH-)
Electrons Oxygen Water Charged Ion
ANODECATHODE Electron transport
Corrosion productsOxygen.O2
HydroxideOH-
Metal ions dissolve
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CorrosionFactors Oxygen corrosion
• Can be found throughout the system• Mechanism same as other oxygen corrosion cells• Corrosion mechanisms affected by:
– pH• Minimize corrosion: pH >9.0
– Temperature• Higher temperatures reduce O2 solubility, but
significantly increase corrosivity
– Dissolved oxygen concentration• Higher O2 concentrations increase corrosivity
– Fluid velocity• Enhances effect of other corrodents• More diffusion - better mass transport
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CorrosionOxygen Corrosion
Dissolved oxygen as function of temperature at atmospherical pressure
5.5 ppm O2
2.5 ppm O2
85°C (185 °F)
50°C (122 °F)
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CorrosionOxygen Corrosion
Problems associated with oxygen:
• Crack formation in degassers - deaerator cracking• Corrosion pits that require immediate remedy to
obtain approval after periodic inspections by authorities
• Corrosion damage to gray cast iron in feed water pumps
• Leaking feed water pipes, leaking economisers, pits and craters in boiler tubes (low pressure boilers)
Oxygen corrosion in feed water line
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CorrosionOxygen Corrosion
Economical impact of oxygen corrosion• Increased energy consumption
– Oxygen corrosion introduces additional iron and copper oxides in the water
• Deposition on heated surfaces (limiting heat transfer)
– Increased blowdown due to turbidity water – Increased conductivity due to addition of oxygen
scavengers (e.g. sulfite) requires increased blowdown
Oxygen corrosion in feed water line (pH
7.5. 50 °C)
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CorrosionCaustic Damage
There are two forms of damage caused by caustic soda to high pressure boilers, namely:
– Caustic corrosion– Caustic embrittlementDo we have a
picture Steef??
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CorrosionCaustic Corrosion
• Two conditions are necessary for caustic corrosion to occur:
– Presence of a corrosive material in the boiler water (caustic soda)
– Mechanism for concentrating this material, usually due to deposits
• Usually found only in high pressure boilers
Fe3O4 Fe2O3 + FeO (Magnetite dissolution)Fe2O3 + 2 NaOH 2 NaFeO2 + H2O (soluble)FeO + 2 NaOH Na2FeO2 + H2O (soluble)
• Localized in boiler• Also called crater attack or caustic gouging• No embrittlement of metal
Do we have a picture Steef??
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CorrosionCaustic Embrittlement
Embrittlement is a special form of stress corrosion cracking• Should not be confused with caustic corrosion
• Three conditions must be present– Concentrating mechanism present– Metal under high stress– Must contain silica
• Inhibited by improved fabrication techniques and by organic and nitrate-based inhibitors
Steef, kan deze slide eruit? Zo
nee, do we have a picture Steef?
Check last remark!!
Nitrate??!?
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CorrosionConcentration mechanism
Steam blanketing
Under deposit / concentration to dryness• Excessive heat input• Insufficient coolant flow• Deposits
Elongated gouge caused by steam blanketing
NaOH
NaOH
NaOH
Fe3O4 porous deposit
Water In
Steam Out
NaOH
NaOH
Magnetite
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CorrosionConcentrating Mechanisms
The following conditions can result in dangerously high localized caustic soda concentrations
• (Porous) metal oxide deposits• Operation above rated capacity• Excessive rate of load increase • Excessive localized heat input• Localized pressure differentials• Restrictions in generating tube(s)
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CorrosionAcid corrosion
Causes of acidity• Feedwater acid contamination• Acid leaks from demineralizer, e.g. acid regenerant • Breakdown of organic materials• Condenser leaks
– MgCl2 + 2 H2O Mg(OH)2 + 2 HCl• Organic chlorides
– R-X + 2 H2O R-OH + HCl
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CorrosionAcid corrosion
Special form of acid corrosion can be found in condensate system:
Alkalinity of BFW breaks down in Boiler • 2 NaHCO3 Na2CO3 + CO2 + H2O
Na2CO3 + H2O 2 NaOH + CO2
CO2 leaves with steam and reacts with condensed water droplets to Carbonic Acid • CO2 + H2O H2CO3
The H2CO3 acid attacks metals by reducing pH
% C
on
vers
ion
Pressue (bar)
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Steam purity
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Steam PurityWhat is
Defined as the amount of non-water components of the steam• Priming• Foaming• Misting• Selective carry-over
Normally measured in terms of ppb sodium ion and ppb silica.• Sodium Limits to turbines
– Old industrial turbines - max. of 20 ppb– New industrial turbines - max. 5 ppb
• Silica Limits to Turbines - 20 ppb
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Steam PurityProblems caused
Effects of low steam purity• Process Contamination • Loss of Turbine Efficiency• Turbine Imbalance• Operational Problems• Plant Shut-down
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Water Quality guidelines
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Water quality guidelines
Boiler Water component [ppm]
Drum Pressure. psig (bar)
150 (10) 300 (20) 600 (40) 900 (60) 1200 (80) 1500 (100)
TDS (max) 4000 3500 3000 2000 500 300
Phosphate (as PO4)
30-60 30-60 20-40 15-20 10-15 5-10
Hydroxide (as CaCO3)
300-400 250-300 150-200 120-150 100-120 80-100
Sulfite 30-60 30-40 20-30 15-20 Not recommended
Not recommended
Silica (as SiO2. max)
100 50 30 10 5 3
Total Iron (as Fe. max)
10 5 3 2 2 1
Organics 70-100 70-100 50-70 50-70 50-70
Drum-type boilers using softened (not deionized) feedwaters
Different for all boiler types. feed water quality and region
•ASME: USA
•Krachtwerktuigen: Holland
•TUV: Germany
•British Standard: UK
Check Etienne – source???
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Water quality guidelinesHigh purity Feed water
Boiler Water Component
Drum pressure psig (bar)
Upto 600 (40)
900 (60) 120 (80) 1500 (100) 1800 (120) 2400 (160)
TDS (max) 500 500 300 200 100 50
Phosphate (as PO4)
15-25 15-25 15-25 5-10 5-10 5-10
pH 9.8-10.2 9.8-10.2 9.8-10.2 9.4-9.7 9.4-9.7 9.4-9.7
Silica (as SiO2. max)
10 10 5 2 1 0.25
Total iron (as Fe. max)
2 2 2 1 0.5 0.25
Hydrazine Idem soft water
0.04-0.06 0.04-0.06 0.04-0.06 0.04-0.06 0.04-0.06
Drum-type boilers using high purity (deionized) feedwaters
Different for all boiler types. feed water quality and region
•ASME: USA
•Krachtwerktuigen: Holland
•TUV: Germany
•British Standard: UK
Check Etienne – source???
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Water quality guidelinesgeneral remarks
• Limits on TDS will vary with the design of the boiler and with the needs of the system
• Despite TDS maximums. industrial type boilers (as opposed to utility type) should not be operated above 100 cycles of concentration
• Silica may be carried at higher levels if there are no condensing turbines in the cycle. In any case. maintain an "O"/SiOratio of at least 3/1 to inhibit silica deposition.
• Iron levels shown are theoretical levels based on feedwater iron multiplied by cycles of feed water concentration
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ASME Guidelines for Feedwater Quality
Boiler Pressure [bar]
Boiler Pressure [psi]
Hardness [ppm]
I ron [ppm]
Copper [ppm]
0 - 20 0 – 300 0.300 0.100 0.050
21 - 31 301 – 450 0.300 0.050 0.025
32 - 41 451 – 600 0.200 0.030 0.020
42 – 51 601 – 750 0.200 0.025 0.020
52 – 62 751 – 900 0.100 0.020 0.015
63 - 103 901 – 1500 N/D 0.010 0.010
Fire tube
0 - 20 0 – 300 1.0 0.100 0.050
Water tube
Make again in PPT format
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Feedwater Quality requirementsFrance - Softened Feedwater
Operating pressure
bar < 15 15 - 25 25 - 35 35 – 45
Feedwater
pH ≥ 8.5 ≥ 8.5 ≥ 8.5 ≥ 8.5
Total Hardness [°F] < 0.5 < 0.2 < 0.2 < 0.1
Oxygen remove remove Remove Remove
Huil absent absent absent Absent
Boiler water
TAC [°F] ≤ 100 ≤ 80 ≤ 60 ≤ 40
TA [°F] 0.7 TAC 0.7 TAC 0.7 TAC 0.7 TAC
Silica [Mg/L] ≤ 200 ≤ 150 ≤ 90 ≤ 40
SiO2 / TAC ≤ 2.5 ≤ 2 ≤ 1.5 ≤ 1
Total dissoloved solids
[Mg/L] < 4000 < 3000 < 2000 < 1500
Chlorine [Mg/L] ≤ 800 ≤ 600 ≤ 400 ≤ 300
Phosphate [Mg/L] 30 - 100 30 - 100 20 - 80 20 – 80
pH 10.5 - 12 10.5 - 12 10.5 - 12 10.5 - 12
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Feedwater Quality requirementsFrance - Demineralized Feedwater
Operating pressure
bar 40 - 60 60 - 75 75 - 100
Feedwater
pH ≥ 8.5 ≥ 8.5 ≥ 8.5
Total Hardness [°F] < 0.05 < 0.05 < 0.05
Oxygen remove remove Remove
Huil Mg/l < 0.05 < 0.05 < 0.05
Iron Mg/l < 0.05 < 0.05 < 0.03
Copper Mg/L < 0.03 < 0.03 < 0.01
Boiler water
TAC [°F] ≤ 25 ≤ 10 ≤ 5
TA [°F] ≥ 0.5 TAC ≥ 0.5 TAC ≥ 0.5 TAC
Silica [Mg/L] ≤ 15 ≤ 10 ≤ 5
SiO2 / TAC < 1 < 1 < 1
Total dissoloved solids
[Mg/L] < 500 < 300 < 100
Free NaOH [Mg/L] < 20 < 300 < 100
Phosphate [Mg/L] 10 - 60 10 - 40 5 – 20
pH 10 - 11 10 - 11 9.5 – 10.5
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Feedwater Quality requirementsFrance – Fire tube boilers
Operating pressure
bar ≤ 10 10 - 15 15 – 25
Feedwater
pH ≥ 8.5 ≥ 8.5 ≥ 8.5
Total Hardness [°F] < 0.5 < 0.5 < 0.2
Oxygen remove remove Remove
Huil Mg/l absent absent Absent
Boiler water
TAC [°F] ≤ 120 ≤ 100 ≤ 80
TA [°F] 0.7 TAC 0.7 TAC 0.7 TAC
Silica [Mg/L] ≤ 200 ≤ 200 ≤ 150
SiO2 / TAC ≤ 2.5 ≤ 2.5 ≤ 2
Total dissoloved solids
[Mg/L] ≤ 5000 ≤ 4000 ≤ 3000
Free NaOH [Mg/L] < 20 < 300 < 100
Phosphate [Mg/L] 30 - 100 30 - 100 30 - 100
pH 10.5 - 12 10.5 - 12 10.5 - 12
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Feedwater Quality requirementsGermany - VGB
Scope Continuous operation
Continuous operation
Continuous operation
Continuous operation Continuous operation
Fully demineralized feedwater
Demineralized feedwater
Demineralized feedwater
Demineralized feedwater
Steam for condensing turbines
Alkalized boiler water – Na3PO4 recommended
Alkalized boiler water – Na3PO4 recommended
Volatile agents
Pressure area [bar] > 68 68 - 136 > 136
PH (25 °C)Neutral operationCombined operationAlkaline operation
7-88-99-10
9.8 – 10.2 9.3 – 9.7 Alkaline
Conductivity (25 °C) [uS/cm] < 0.25 < 50 < 50 < 5 (for < 250 kW/m2)< 3 (for > 250 kW/m2)
< 0.2
Oxygen
Neutral operation
Combined operation
Alkaline operation
[mg/l]
0.050 - 0.2500.030 – 0.150< 0.100
Iron [mg/l]
Copper [mg/l] < 0.02< 0.03
< 0.020< 0.030
Na [mg/l] < 0.01 < 0.010
Silica [mg/l] < 0.02 < 0.020
If Na3PO4 is dosed PO4 [mg/L] <6 <3 NA
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Boiler water Quality requirementsGermany - TÜV
Scope Softened feedwater
Boiler water on softened feedwater Demin. feedwater
Boiler water based on demin. feedwater
Pressure area [bar] 1 <> 68 1 <> 22 22 <> 44 44 <> 68 < 68 < 68 < 68
Appearance Colourless, free from suspended matter
Conductivity (25 °C) [µS/cm] < 10,000 < 5,000 < 2,500 < 0.2 < 150 < 3
Hardness [ppm CaCO3] < 1.0
Oxygen ppm < 0.02 < 0.1
Phosphate [mg/l ] 10 – 20 5 - 15 5 - 15 < 6
PH (25 °C) 10.5 – 12 10 – 11.8 10 – 11 > 9 9.5 – 10.5 > 7
p-alkalinity [ppm CaCO3] 50 – 600 25 - 300 5 – 50
CO2 fixed [mg/l ] < 25
Iron ppm < 0.03 < 0.03
Copper Ppm < 0.005 < 0.005
Silica [mg/l] NR Graph Graph < 10 < 0.02 < 4 < 4
Organic carbon [ppm as KMnO4] < 10 < 3
Oil ppm < 1 < 1
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Boiler water Quality requirementsItaly
Scope
Pressure area [bar]
Appearance
Conductivity (25 °C) [µS/cm]
Hardness [ppm CaCO3]
Oxygen ppm
Phosphate [mg/l ]
PH (25 °C)
p-alkalinity [ppm CaCO3]
CO2 fixed [mg/l ]
Iron ppm
Copper Ppm
Silica [mg/l]
Organic carbon [ppm as KMnO4]
Oil ppm
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Boiler water Quality requirementsSpain – Firetube: UNE 9-075-92
Feedwater Feedwater Boiler water Boiler water Boiler water
≤ 0.5 bar > 0.5 bar ≤ 0.5 bar 0.5 <≥ 13 bar > 13 bar
Appearance Colourless and without suspended solids
Hardness [ppm CaCO3] ≤ 10 ≤ 5
Oxygen [mg/L] - ≤ 0.2
PH (20 °C) 8-9 8-9 10.5 – 12.5 10 - 12 10 – 12
CO2 fixed [mg/l ] ≤ 25 ≤ 25
Organic carbon [ppm as KMnO4] ≤ 10 ≤ 10
Oil ppm ≤ 3 ≤ 1
Conductivity (≤ 40 kg/m2) [mg/L] ≤ 6,000 ≤ 6,000 ≤ 4,000
Conductivity (> 40 kg/m2 [mg/L] ≤ 5,000 ≤ 5,000 ≤ 3,000
p-alkalinity [ppm CaCO3] ≤ 1,000 ≤ 800 ≤ 600
Phosphate [mg/l P2O5 ] ≤ 30 ≤ 25 ≤ 20
Silica [mg/l SiO2] ≤ 250 ≤ 200 ≤ 150
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Boiler water Quality requirementsSpain - water tube: UNE 9-075-92
Maximum allowed values
Hardness Alkalinity TSS pH (20 °C) Phosphate Silica
[mg/L] [mg/L] [mg/L] [Mg/L P2O5] [mg/l]
< 20 Natural circulation 3,500 700 150 9.5 - 11 25 140
21- 32 Natural circulation 3,000 600 100 9.5 - 11 25 50
33 – 40 Natural circulation 2,500 500 80 9.5 - 11 10 50
41 – 53 Natural circulation 2,000 400 60 9.5 - 11 10 50
54 – 64 Natural circulation 1,500 300 40 9.5 - 11 10 10
65 – 70 Natural circulation 1,250 250 20 9.5 - 11 3 10
71 – 126 Natural circulation 100 100 10 9.5 – 10.5 3 4
127 – 165 Natural circulation 50 40 9.5 – 10.5 3 4
166 – 180 Natural circulation 25 10 9.5 – 10.5 3 4
181 – 203 Natural circulation 15 2 9.5 – 10.5 3 4
> 98 Forced circulation 0.05 9.5 – 10.5 3 4
< 20 Forced circulation with continuous steam formation
2,000 400 100 - - 140
20 - 40 Forced circulation with continuous steam formation
1,000 200 50 - - 50
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Boiler water Quality requirementsNetherlands
Parameters
Krachtwerktuigen KEMA
Waterpijp Low pressure boilers
Pressure area [bar] 0.5-20 <80
Phosphate [mg/l ] 30-80 <15
PH (25 °C) 9.8-10.2
p-alkalinity [ppm CaCO3] 250-750
Chloride [mg/l] <2
Silica [mg/l] <5
TDS
Conductivity [µS/cm] < 6000 (pH=8.3) <2500 (after cation filter)
Organic carbon [ppm CZV] <150
Iso ascorbic acid [mg/l]
CHECK
I do not have the original!
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Boiler water Quality requirementsUK – Shell tube upto 30 bar
Parameter Unit Feedwater Boiler water Boiler water
Demineralized feedwater
Heat flux ≤ 300 > 300
Appearance Clear, no foam
pH (25 °C) 8.5 – 9.5 10.5 – 12.0 9.5 – 10.5
Total Hardness Mg/kg CaCO3 ≤ 2
Oxygen Mg/kg
Total M-alkalinity Mg/kg CaCO3 ≤ 1000 ≤ 100
O- and P-alkalinity Mg/kg CaCO3 ≥ 350 ≥ 20
Oil and grease Mg/kg ≤ 1
Oxygen scavengerSulfite, orHydrazine, orTannin, orIso ascorbic acid, orDEHA
Mg/kg30 – 700.1 – 1.0120 – 16015 – 300.1 – 1.0 (FW)
Assess0.1 – 1.0AssessAssess0.1 –1.0 (FW)
Phosphate Mg/kg 30 – 60 10 – 30
Silica Mg/kg ≤ 150 ≤ 5
Suspended solids Mg/kg ≤ 200 ≤ 20
Dissolved solids Mg/kg ≤ 3500 ≤ 1000
Conductivity (25 °C) uS/cm ≤ 7000 ≤ 2000
CHECK
Is there an update, have
seen the draft!
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Boiler water Quality requirementsUK – Fired Water tube
Parameter Unit 0 - 20 21 – 40 41 - 60 61 - 80 81 - 100 101 - 120 ≥ 121
Feedwater
pH (25 °C) 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5
Total Hardness Mg/kg CaCO3 2 1 ND ND ND ND ND
Oxygen Mg/kg ≤ 0.02 ≤ 0.02 ≤ 0.01 ≤ 0.005 ≤ 0.005 ≤ 0.005 ≤ 0.005
Fe, Cu, and Ni Mg/kg ≤ 0.05 ≤ 0.05 ≤ 0.03 ≤ 0.02 ≤ 0.02 ≤ 0.02 ≤ 0.02
Boiler water
O- and P-alkalinity Mg/kg CaCO3 50 - 300 50 - 150 25 – 50 10 – 20 5 - 10 2 - 5 1 - 5
Oxygen scavengerSulfite, orHydrazine, orTannin, orIso ascorbic acid, orDEHA in FW
Mg/kg30 – 500.1 –10120 – 16015 – 300.1 – 0.25
20 – 400.1 –0.5NR15 – 300.1 – 0.25
15 - 200.1 –0.2NR15 – 300.1 – 0.25
NR0.05 –0.1NRNR0.1 – 0.25
NR0.05 –0.1NRNR0.1 – 0.25
NR0.05 –0.1NRNR0.1 – 0.25
NR0.05 –0.1NRNR0.1 – 0.25
Chloride Assess Assess Assess Assess
Phosphate Mg/kg 30 – 70 20 – 50 20 – 40 15 – 30 10 – 20 3 – 10 3 – 5
Silica Mg/kg ≤ 0.4 x O & P alkalinity
≤ 0.4 x O & P alkalinity
≤ 20 ≤ 5 ≤ 2 ≤ 1.5 ≤ 0.5
Dissolved solids Mg/kg ≤ 3000 ≤ 2500 ≤ 1000 ≤ 200 ≤ 50 ≤ 20 ≤ 10
Conductivity (25 °C) uS/cm ≤ 6000 ≤ 5000 ≤ 2000 ≤ 450 ≤ 150 ≤ 60 ≤ 35
CHECK - Is there an update, have seen the draft!
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Boiler water Quality requirementsUK – Other boilers
Non-fired Water Tube
Non-fired Water Tube
Non-fired Water Tube
Once through
Coil boiler Coil boiler Electrode boiler
Parameter Unit 0 - 40 41 - 80 > 80 < 40 > 41 101 – 120
Feedwater
pH (25 °C) 9.3 – 9.8 9.3 – 9.8 9.3 – 9.8 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 7.5 – 9.5
Total Hardness Mg/kg CaCO3 ND ND ND ≤ 1 ND ≤ 1
Oxygen Mg/kg ≤ 0.02 ≤ 0.01 ≤ 0.005 ≤ 0.005 Nil
Fe, Cu, and Ni Mg/kg ≤ 0.05 ≤ 0.03 ≤ 0.02 ≤ 0.005 ≤ 0.02 ≤ 0.2
Cond ≤ 400
Boiler water
O- and P-alkalinityTotal
Mg/kg CaCO3 25 - 50 10 - 50 2 – 5 ≥ 300 ≥ 150 ≥ 300≤ 600
Oxygen scavengerSulfite, orHydrazine, orTannin, orIso ascorbic acid, orDEHA in FW
Mg/kg15 - 200.1 –0.5120 – 16015 – 300.1 – 0.25
-0.05 –0.1NR15 – 300.1 – 0.25
-0.05 –0.1NR15 – 300.1 – 0.25
10 - 200.05 –0.1NRNR0.1 – 0.25
NR0.02 –0.05NRNR0.02 – 0.05
50 – 100
pH > 9.5Hardness 0 - 10
Phosphate Mg/kg 20 - 40 15 – 30 3 – 10 Assess 3 - 5
Silica Mg/kg ≤ 20 ≤ 5 1 - 5 ≤ 0.02 < 0.4 X O&P alk < 0.4 X O&P alk
Dissolved solids Mg/kg ≤ 1000 ≤ 200 ≤ 50 ≤ 200 ≤ 8000 ≤ 5000
Conductivity (25 °C) uS/cm ≤ 2000 ≤ 400 ≤ 100 ≤ 0.2 400 – 2000
CHECK - Is there an update, have seen the draft!
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Boiler water Quality requirementsUK – Fired Water tube
Parameter Unit 0 - 20 21 – 40 41 - 60 61 - 80 81 - 100 101 - 120 ≥ 121
Pressure bar ≤ 300
Appearance Clear, no foam
pH (25 °C) 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5 8.5 – 9.5
Total Hardness Mg/kg CaCO3 2 1 ND ND ND ND ND
Oxygen Mg/kg ≤ 0.02 ≤ 0.02 ≤ 0.01 ≤ 0.005 ≤ 0.005 ≤ 0.005 ≤ 0.005
Fe, Cu, and Ni Mg/kg ≤ 0.05 ≤ 0.05 ≤ 0.03 ≤ 0.02 ≤ 0.02 ≤ 0.02 ≤ 0.02
Feedwater