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Boiler Water Best Practises
Boiler Water Best Practises
Boiler Water
Internal Treatment
Technology
Why is Effective Internal Boiler
Water Treatment Necessary ?
Effective Internal Boiler Water
Treatment
Controls
• Deposition
• Corrosion
• Carryover
and
Enhances System Reliability
and Efficiency
• Avoids unscheduled shutdowns
• Helps ensure uninterrupted production
• Reduces maintenance costs
• Reduces operating costs
What Operating Costs are
Associated with Boiler
Operation ?
Boiler Operating Costs
• Fuel - Gas, Oil, Coal
• Water - Influent and Effluent
• Regenerants - Salt, Acid,
Caustic
• Water Treatment
• Fuel - Gas, Oil, Coal
• Water - Influent and Effluent
• Regenerants - Salt, Acid, Caustic
• Water Treatment
Boiler Operating Costs
• Need to minimise all operating costs
Reducing boiler water blowdown gives
water, energy and chemical savings
• Need to maximise efficiency
Maintain clean heat transfer surfaces
Heat recovery systems
Boiler Operating Costs
Effective Internal Boiler Water
Treatment
Controls
•
Deposition
Boiler Water Deposit Control
• Hardness salts
• Calcium
• Magnesium
• Metal oxides
• Iron
• Copper
Comparison of Heat Transfer Surfaces
With and Without Deposits
Fireside Waterside Fireside Waterside
Metal Metal Scale
Without deposits With deposits
600°F
500°F 500°F
800°F
and
above
Energy Loss from Scale Deposits
(from Energy Conservation Programme Guide for Industry & Commerce)
1
64
1
32
3
64
1
16
5
64
3
32
0
Scale Thickness, inches or mm
Energy
Loss
%
8
7
6
5
4
3
2
1
I
r
o
n
&
S
i
l
i
c
a
S
c
a
l
e
High
Iron
Content Scale
"Normal" Calcium
Carbonate Scale
0.4 mm 0.8 mm 1.2 mm 1.6 mm 2.0 mm 2.4 mm
Long Term Overheating
Boiler Water Deposit Control
• Removal of impurities
• Pretreatment plant
• Chemical treatment
• Controlled blowdown
Effective Internal Boiler
Water Treatment
Controls
• Deposition
• Corrosion
Boiler Water Corrosion Control
• Oxygen pitting
• Caustic corrosion
• Embrittlement or gouging
• Acidic attack
Oxygen Corrosion - Pitting
Caustic Gouging
Acid Corrosion
Acid Corrosion
Effective Internal Boiler
Water Treatment
Controls
• Deposition
• Corrosion
• Carryover
Control of Boiler Water Carryover
• Effective mechanical steam separation
• Proper control of boiler water chemistry
• Antifoam, as needed
• Avoid major contaminant ingress
• Proper boiler operating practices
What Types of
Internal Boiler Water
Treatments are
Available ?
Internal Treatment
Programmes
General Classifications
• Precipitating
• Solubilising
• Combination
• Phosphate/Polymer
• Phosphonate/Polymer
• Chelant/Polymer
• Phosphate/Chelant/Polymer
• All Polymer
• Coordinated pH/Phosphate/Polymer
• All Volatile Treatment (AVT)
Internal Treatment
Programmes
Boiler Water Polymers
are Crucial to the
Success of any
Internal Treatment
Programme
How do Boiler Water Polymers
Function ?
Boiler Water
Polymers
The mechanisms by which boiler
water polymers function are
• Complexation / Solubilisation
• Crystal modification
• Dispersion
Calcium phosphate,
magnesium silicate
crystals formed in
boiler water without
dispersant
Calcium phosphate,
magnesium silicate
crystals formed in
boiler water in the
presence of a
sulphonated polymer
Variables Affecting Polymer
Performance
• Functional group
• carboxylated (SCP/SCCP)
• sulfonated (SSP)
• phosphorylated (HTP)
• Polymer backbone
• Molecular weight
CH3
O-
Polymethacrylate
X
C CH2
C=O
CH
O-
CH2
Polyacrylate
C = O
X
CH2
OH
CH
Acrylate-Acrylamide Copolymer
CH2
NH2
CH
X
C = O
C = O
CH2
SO3
-
CH
Sulfonated Styrene-Maleic
Anhydride Copolymer
CH CH
C
X Y
C =
O
O
O
=
Typical Polymer Structures
O-
O-
Phosphonate
P = O
Poly (isopropenyl phosphonic acid)
PIPPA
O P
C
CH3
OH
X
O-
CH2
=
R
HEDP
P
- O
O
C P
CH3
OH
O
O -
- O
O -
=
=
Polyethylene glycol allyl ether (PEGAE)
CH2 CH
C = O
O- H+
CH2 CH
CH2
O [CH2 CH2 O]m
H
n
Typical Polymer Structures
Polymer Performance
vs
Molecular Weight
Polymer Molecular Weight
Deposition
Programme Selection
Considerations
• Boiler pressure, design
• Pre-treatment plant type
• Feedwater quality
• Hot well, deaerator type
• Steam turbine
• Control capabilities
Chemical Factors
• Total Dissolved Solids (TDS)
• Alkalinity
• Silica
• Suspended Solids
ASME Boiler Feedwater Quality
Guidelines for Modern Industrial
Water-Tube Boilers
•
Drum Pressure
•
(kg/cm²)
•
0 - 21
•
22 - 31
•
32 - 42
•
43 - 52
•
53 - 63
•
64 - 70
•
71 - 105
Iron
(ppm Fe)
0.10
0.05
0.03
0.025
0.02
0.02
0.01
Copper
(ppm Cu)
0.05
0.025
0.02
0.02
0.015
0.015
0.01
Hardness
(ppm CaCO3)
0.30
0.30
0.20
0.20
0.10
0.05
0.0
Internal Treatment
Programmes
• Phosphate/Polymer
Phosphate/Polymer Treatment
• Reactions:
• Ca + PO4 + OH
Ca(OH)PO4
• Calcium Phosphate Hydroxide
Hydroxyapatite
•
• Mg + SiO3 + OH
Mg(OH)SiO3
• Magnesium Silica Hydroxide Serpentine
Phosphate/Polymer Treatment
Characteristics
• Hardness controlled by precipitation
• Polymers used to control hardness
sludge and metal oxides
• Phosphate residual used for programme
control
• Hydroxide alkalinity required (pH : 10.5 -
12)
Phosphate/Polymer
Treatment
Boiler Control Parameters
• Phosphate residual as PO4 depending on
hardness in the feedwater
• usually associated with boiler pressure
• and environmental legislation
• M alkalinity of 700 ppm as CaCO3 (25 % of
TDS)
• Polymer : min 360 ppm as SP8100
• Still the most used method for treating low
pressure boilers
Phosphate/Polymer
Treatment
• Disadvantages
• Is a precipitation
programme (some
deposition is normal)
• Higher blowdown rates
may be required
Advantages
• Tolerates a wide range of
feedwater hardness
• Non corrosive treatment
• Suitable for low to medium
pressure systems
• Easy operator control
Internal Treatment Programmes
• Phosphate/Polymer
• Phosphonate/Polymer
Phosphonate/Polymer
Characteristics
• Organic phosphor donors combined
with three synergistic polymers
• Complexes hardness, iron and copper
ions in BFW
• Disperses/solubilises contaminants in
boiler minimising sludge formation
Phosphonate/Polymer
– 200 - 300 ppm in blowdown
– (BFW hardness + tot Fe) max 1 ppm for
300 ppm in boiler
– filtered tot. PO4 min 6 ppm in BD
– Other :
• conductivity
• SiO2
• M-alk
a) Solubilising
Boiler Control Parameters
b) Precipitating
• Phosphate residual as PO4 depending on
hardness in the feedwater
• M alkalinity of 700 ppm as CaCO3 (25 % of
TDS)
Phosphonate/Polymer
Boiler Control Parameters
Internal Treatment
Programmes
• Phosphate/Polymer
• Phosphonate/Polymer
• Chelant/Polymer
Chelant/Polymer
Treatment
• Common Chelating Agents
• EDTA
• NTA
Chemical Structure of
EDTA
- OOC - CH2
- OOC - CH2
N - C - C - N
H
CH2 - COO -
CH2 - COO -
H
H H
EDTA/Calcium Complex
Ca
CO
N
N
CH2
CH2
CH2
CH2
CH2
CH2
CO
CO
CO
O
O
O
O
Chelant/Polymer Treatment
Characteristics
• Are solubilising treatments
• Chelant complexes hardness and soluble iron /
copper
• Polymers used to enhance metal oxide control
• Must be fed to the feedwater line
Chelant/Polymer Treatment
• Disadvantages
• Requires intensive
operator control
• Potentially corrosive if
misapplied
Advantages
• Solubilising treatment
• Effective on hardness and
soluble iron
• Allow reduced blowdown
• Increased reliability and
efficiency
• Suitable for low to medium
pressure systems
Internal Treatment
Programmes
• Phosphate/Polymer
• Phosphonate/Polymer
• Chelant/Polymer
• Phosphate/Chelant/Polymer
Chelant/Phosphate/Polymer
Treatment
Characteristics
• Utilises EDTA chelant (partial chelation)
• Primarily a solubilising programme
• Phosphate provides back-up upset protection
• Residual phosphate test used as programme control
• Polymers used to control metal oxides and other
precipitates
Chelant/Phosphate/Polymer
Treatment
• Disadvantages
• Some precipitation is
possible
• Potentially corrosive
if misapplied
Advantages
• Primarily a solubilising treatment
• Effective on hardness and iron
• May allow reduced blowdown
• Increased reliability and
efficiency
• Easy and accurate control test
• Tolerates a wide range of
feedwater hardness
• Suitable for low to medium
pressure systems
Internal Treatment
Programmes
• Phosphate/Polymer
• Chelant/Polymer
• Phosphate/Chelant/Polymer
• All Polymer
All Polymer Treatment
Characteristics
• Certain polymers can be effective
complexing agents
• Principle mechanism is complexation of
soluble impurities
• Secondary mechanism is dispersion of
particulates
• Fed to the boiler feedwater
Limitations of Polyacrylate Based
All Polymer Programmes
• Low tolerance to feedwater quality upsets
• Potential for calcium polyacrylate deposition
• Releases ammonia
• Economiser iron pick-up
• Precise testing for polymers is difficult
Internal Treatment
Programmes
• Phosphate/Polymer
• Phosphonate/Polymer
• Chelant/Polymer
• Phosphate/Chelant/Polymer
• All Polymer/OptiSperse AP
What is OptiSperse AP ?
• A new, revolutionary programme using
patented co-polymer technology
• A stand-alone all polymer / all organic boiler
internal treatment programme which
provides superior control over hardness and
iron deposition
OptiSPerse AP Treatment vs.
Traditional All Polymer
• Traditional All Polymer
Programme
• Generates ammonia
• Forms calcium-polymer
deposits with BFW
hardness excursions or
underfeed
• Overfeed may cause
foaming
• Corrosive to economiser
surfaces
• Must be fed downstream of
copper alloys
• OptiSperse AP
Programme
• No ammonia generated
• No treatment related
deposition
• No steam purity
problems
• Not corrosive to preboiler
circuit
• May be fed ahead of
copper alloys in BFW
Research Boiler Studies Under Fouling
Conditions
Test Conditions
900 psig (63 kg/cm2)
All-polymer Programme
Ca/Mg/Fe present
TRADITIONAL
ALL-POLYMER
OPTISPERSE AP
0 1 2 3 4 5
POLYMER/HARDNESS RATIO
DWD
Research Boiler Studies
Under Potential Fouling Conditions
(Equal Polymer Actives)
300 psig (21 kg/cm2) 600 psig (42 kg/cm2) 900 psig (63 kg/cm2)
Deposit
Weight
Density
OPTISPERSE AP Traditional All-Polymer
Internal Treatment
Programmes
• Phosphate/Polymer
• Phosphonate/Polymer
• Chelant/Polymer
• Phosphate/Chelant/Polymer
• All Polymer
• Coordinated
pH/Phosphate/Polymer
Coordinated pH/Phosphate
Polymer Treatment
Characteristics
• Primarily for high purity/high pressure
systems
• Mainly a corrosion control programme
• Phosphate used to control pH and neutralise
excess caustic
• Polymers used to control deposition
Corrosion of Mild Steel vs. pH
1 2 3 4 5 6 7 8 9 10 11 12 13 14
Safe Range
Relative
Corrosive
Attack
8.5 pH 12.7 pH
Caustic Concentration
Mechanism
Magnetite
NaOH
Steam Out
NaOH
Boiler Water in
Fe3O4 Porous
Deposit
NaOH
NaOH
NaOH
NaOH
Boiler water in
steam
escapes
porous
deposit
magnetite
Na+
HPO4
2 -
Na+
Na+
Na+
Na+
Prevention
HPO4
2 -
HPO4
2 -
HPO4
2 -
HPO4
2 -
Minimising Caustic
Concentration and Corrosion
using Phosphate
NaOH + Na2HPO4 Na3PO4 + H2O
Caustic
Soda
Disodium
Phosphate
Trisodium
Phosphate
Water
Co-ordinated Congruent Phosphate/pH
Control Chart
2.6:1 Na/PO4
8.2
8.4
8.6
8.8
9.0
9.2
9.4
9.6
9.8
10.0
10.2
10.4
10.6
10.8
10
2 3 4 5 6 7 8
1 15 20 30 40 50 60
Ortho-phosphate, as PO4 mg/l
"Free" Caustic
Region
Maximum Boundary 3.0:1 Na/PO4
Molar Ratio
Control Boundary 2.2:1 Na/PO4
Molar Ratio "Captive"
Alkalinity
Region
2.7:1 Na/PO4
2.8:1 Na/PO4
pH
Vector
Control
Diagram
T
r
i
-
S
o
d
i
u
m
P
h
o
s
p
h
a
t
e
Caustic
M
ono-Sodium
Phosphate
Blowdown
Di-Sodium
Phosphate
Internal Treatment
Programmes
• Phosphate/Polymer
• Phosphonate/Polymer
• Chelant/Polymer
• Phosphate/Chelant/Polymer
• All Polymer
• Coordinated pH/Phosphate/Polymer OptiSperse
HTP
Characteristics of HTP-2
• A unique new phosphorylated boiler polymer
• Particularly effective on iron
• Demonstrated clean-up ability
• Designed for high purity/high cycles systems
• Suitable for use up to 125 kg/cm²
HTP-2 Polymer Structure
O P
C
CH3
OH
X
O-
CH2
=
Poly (isopropenyl phosphonic acid) . . . PIPPA
Internal Treatment
Programmes
• Phosphate/Polymer - OptiSperse PO, OptiGuard MCP
• Phosphonate/Polymer - OptiSperse PQ
• Chelant/Polymer - OptiSperse CL
• Phosphate/Chelant/Polymer - OptiSperse CP
• All Polymer - OptiSperse AP, OptiGuard MCA
• Coordinated pH/Phosphate/Polymer - OptiSperse HTP
• All Volatile Treatment (AVT)

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