Power Plant Chemistry Ion Exchange Process Prepared By : - Umar Farooq Chemist “A” Chemical Section MSC ( Chemistry ) MBA ( Marketing ) [email protected] [email protected] SEC Shoaiba Jeddah Saudi Arabia 1
Power Plant Chemistry
Ion Exchange Process
Prepared By : -
Umar Farooq Chemist “A” Chemical Section
MSC ( Chemistry ) MBA ( Marketing )
SEC Shoaiba Jeddah
Saudi Arabia 1
Power Plant Chemistry
Table of Content
External Water Treatment
RO Desalination
MSF Desalination
Lime Soda Softening
Zeolite Softening
Demineralization
Weak Cation Resin
Strong Cation Resin
Weak Anion Resin
Strong Anion Resin
Mix Bed
External Water Treatment
It is the removal of impurities from water
out side the ( Condenser ) in power plant
because raw water taken from the river or
sea contain a large number of impurities
with respect to surrounding ,so it is very
necessary to make cleaned and purify the
water before it entrance to wards
( Condenser boiler )
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External Water Treatment
Practically all surface water contain small
amount of mud, clay ,silt ,decayed, vegetation,
Micro Organisms etc.
To obtain required quantity of water
various techniques are applied Such as
Clarification ,Filtration ,Evaporation ,Softening,
Desalination (MSF & RO ) , Ion Exchange , De
Aeration , Aeration Note: External water treatment for Pretreatment System and RO
System already discussed in earlier training module
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What is RO Desalination
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Reverse osmosis is a membrane process where salty source water is supplied under pressure to a semi- permeable
membrane resulting in the passage of fresh water through the membrane prevents the passage of the dissolved minerals
leaving them in the concentrated brine
Seawater supply Pump
D M F
Cartridge
filter
H P Pump
Booster Pump
1st pass R O
E R D
2 nd pass R O 2 nd pass
Feed pump
Permeate
Transfer pump
Potabilisation
Backwash water
Tank
Out fall
To SWCC Shuaibah II
Storage Tank
S MBS
Anti scalant
Anti Scalant
Caustic soda Acid
Coagulant
Polymer
Back wash
7 Umar Farooq Chemist
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What is MSF Desalination
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Multi-stage flash distillation (MSF) is a water desalination process that distill sea water by flashing a portion of the water into steam in multiple stages of what are essentially counter current heat exchangers .Multi-stage flash distillation plants
produce 85% of all desalinated water in the world
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CEP
Sea Water Inlet
Starting Ejector
Brine Heater 1 2 3 4 10 19 20 21 D / A
Duty Ejector 2nd stage Ejectors
I P Steam
After Condenser Inter Condenser Pre Condenser
B V P
1st stage Ejectors
Quick filling
Sea Water Discharge
Make Up
Sea Water Outlet
L P Steam
BRP 1
Cond. Rtn
DP
BRP2
Prodn.
BBDP
Cooling water to
vacuum condensers
The process by which Ca ++ and Mg ++ ion
removed from water is known as water
softening. There are two method is used
Lime soda softening or precipitation
method
Ion exchange method
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Water Softening
Lime soda softening It is the process by which calcium and magnesium salt that cause
hardness in H2O are chemically precipitated and removed by
treatment with lime and soda ash .
Mg(HCO3)2 + 2Ca ( OH) Mg(OH )2 + 2CaCO3+2H2O
Ca(HCO3)2 + Ca(OH) 2CaCO3 + 2H2O
Soluble Insoluble
Most of CaCO3 and Mg(OH)2 from a sludge can be removed by
settling and filtration. So lime can be used for removal of temporary
hardness
MgSO4 + 2Ca ( OH) Mg(OH )2 + 2CaSO4
MgCl2 + 2Ca ( OH) Mg(OH )2 + 2CaCl2
The soluble CaSO4 and CaCl2 are produced and contribute “non carbonated hardness” There must be removed to attain complete
softening of water
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This is done by treating soluble salt of Ca SO4 and CaCl2 with soda
ash ( Na2Co3).when these salt are precipitated as insoluble
carbonate.
CaSO4+Na2CO3 CaCO3+ NaSO4
CaCl2+Na2CO3 CaCO3+ NaCl
Insoluble Soluble
CaCO3 formed is precipitated as sludge the resulting NaSO4 and NaCl
are highly soluble non scale forming
Use of Coagulant in lime soda process
Coagulant serve to agglomerate the particles in softening process
They speed up settling of sludge
Sodium Aluminates has a special advantage as a coagulant in lime
soda softening .practically in reducing magnesium .
Effective use of coagulant to remove silica in the softening process.
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Advantage of Lime soda Softening
Main advantage is reduction of hardness alkalinity TDS
and Silica
Prior Clarification of water in not usually necessary
Reduction of TDS can decrease the conductivity of feed
water, there by decreasing blow down and conserving
heat.
Energy can be saved because of solid reduction in hot
process
With hot process lime soda softening removal of oxygen
and CO2 can be achieved up to same extent
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Disadvantage of Lime soda Softening
The main disadvantage is that while
hardness is remove it is not completely
finished.
Since this process involves adjusting the
amount of lime and soda ash being feed
there fore wide variation in water
composition and flow rate also make
control of this method difficult.
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Ion Exchange Zeolite Softening (Na2Al2Sio2O8.XH2O)
Zeolite softening consist of passing water through a bed of material
that possess the property of removing calcium and magnesium from
water and replacing these ion with sodium or potassium. The
exchange takes place rapidly, so that hard water is passing through
Zeolite bed can be almost completely softened ,regardless of
variation in solution, bicarbonates, sulfate , chlorides etc. Considering only chloride as an example ,for the sake of simplicity
the softening reaction are.
Na2Z+CaCl2 CaZ+ 2NaCl2
Na2Z+MgCl2 MgZ+ 2NaCl2
Material usually applied for this purpose can be naturally occurring
Zeolite I.e. green sand , sulfonated coal or alumina silicate or
synthetic resin based on poly styrene or poly acryllates.
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Advantage of Na2Z Softening
Softened water has low scaling
tendency
Operation is simple and
reliable
Regeneration is easy to handle
Waste disposal is not a
problem
Softener's are easily available
and efficient
Variation in water flow rate up
to large extent have not effect
on treated water quality
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Disadvantage of Na2Z Softening
Softening process has no effect upon alkalinity.
Turbidity and the presence of iron and aluminum
can be deter mental for the ion exchanger.
Strong oxidizing agent like chlorine present in
the water will attack the resin.
At higher pressure and temperature the
exchange capacity of resin is effected.
Zeolite material is unstable in high acidic and
alkaline media
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Demineralization Removal of all kind of ion from water by ion
exchange is called demineralization. Any
salt dissolved in water consist of two types
of ions, +Ve ion called cat ion and -Ve
ion's called anion . In demineralization
process cat ion and anion present in water
are removed one after other by organic ion
exchange resin
The organic resin's are of four
types
Weak Cat ion resin R-COOH Carboxylic group
Strong Cat ion resin R-HSO3 Sulphonic group
Weak anion resin R-NH2OH Phenolic hydroxyl group
Strong anion resin R-NH3OH Amino group
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Ion exchange material
Ion exchange material are either natural or
synthetic. The natural ion exchangers are
termed as Zeolite e.g. green sand aluminous
silicate and sulphonated coal. These can be
regenerated by NaCl solution and are used for
the removal of hardness from water.
Synthetic resins are polymer and co-polymers of
organic compounds like phenol, al dehydes,
styrene's and vinyl derivatives. They differ in
properties due to difference polar group.
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Cat ion Exchangers
Weak Cat ion
This filter bed removers cat ion of salt of weak
acids from water in the following manner e.g. 2RCOO.H + CaSiO3 (RCOO)2 Ca+H2SiO3
2RCOO.H + Ca(HCO3)2 (RCOO)2 Ca+2H2CO3
2RCOO.H + CaCO3 (RCOO)2 Ca+H2CO3
2RCOO.H + Mg(HCO3)2 (RCOO)2 Mg+2H2CO3
2RCOO.H + MgCO3 (RCOO)2 Mg+H2CO3
2RCOO.H + NaHCO3 (RCOO)2 Na+H2CO3
2RCOO.H + NaCO3 (RCOO)2 Na+H2CO3
The water at the outlet of weak cat ion exchanger contain weak acids
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Weak Cat ion Regeneration
Normally 2% HCl is passed
through bed for half hour .All cat ions
that had bed absorbed by resins during
normal service operation are replaced
by H + ion of acid and soluble chlorides
produced in the process of regeneration
are drained to waste
(RCOO)2 Ca + HCl 2RCOOH+CaCl2
Exhausted Resin Regenerated Resin
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Cat ion Exchangers Strong Cat ion
A regenerated strong cat ion resins has
sulphonic functional group (-HSO3) and
removes cat ion of both weak and strong
salts of acids from water as given below. 2RSO3.H + CaSO4 (RSO3)2 Ca+H2SO4
2RSO3.H + CaCl2 (RSO3)2 Ca+2HCl Strong Acid
2RSO3.H + Ca(NO3)2 (RSO3)2 Ca+2HNO3
2RSO3.H + Ca(HCO3)2 (RSO3)2 Ca+2H2CO3 Weak Acid
The water at the outlet of strong cat ion exchanger cat
ion strong acids ( HCl , H2SO4 , & HNO3 )
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Cause of Strong Cat ion Exhaust When strong cat ion filter bed exhausted . It has no H + ion to
exchange with the cat ion (Ca++,Mg+ +,Na+) These cat ion escape in
outlet water. In absence of H + ion . The conductivity of effluent water
decreases and pH is increases , Because H + ion are lightest of all
NaCl escape unchanged form 2nd stage to 3rd stage filter and are
release as NaOH in water
RNH2OH+NaCl RNH2Cl+NaOH
When weak anion filter is exhausted the conductivity
of effluent water increases stately but when strong cat ion resin gets
exhausted. The conductivity of effluent water of weak anion filter
more repaid. It is due to the formation of NaOH is 3rd stage filter by
leaking of Na+ from strong cat ion filter.
Acid Treatment
Fresh 7% HCl solution prepared in deionized water is passed
through the filter almost 40 minute
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Anion Exchanger
Weak anion A regenerated weak anion resin which has amino (-NH2) functional
group will remove all the anions of strong acid from water.
RNH2.OH + HCl RNH2Cl +H2O
RNH2.OH + H2SO4 (RNH2)2SO4 +H2O
RNH2.OH + HNO3 RNH2NO3 +H2O
The water at the outlet of weak anion exchanger will contain only
anion of weak acid . If any e.g. CO32- , SiO3
2- in the form of H2CO3
and H2SiO3
Alkali Treatment
Fresh 3% NaOH solution prepared in deionized water is passed
through the filter almost 70 minute
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Anion Exchanger
Strong anion This filter remove anion of both weak acids and strong acids.
2RNH3.OH + H2CO3 (RNH3)2CO3 +2H2O
2RNH3.OH + H2SiO3 (RNH3)2SiO3 +2H2O
2RNH3.OH + HCl RNH3Cl +H2O
2RNH3.OH + H2SO4 (RNH3)2SO4 +2H2O
Alkali Treatment
4% NaOH is used pass the alkali through the filter for one hour. This
filter is stopped for regeneration when SiO2 content increasing trend.
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Mix Bed Filter
The filter bed contain strong cat ion
The cat ion and anion resin are so
intimately mixed that water following
through the bed may be considered to
have comes across a large number of
small strong cat ion and strong anion
beds. The water at the outlet of mix
bed is of higher quality purity and its
conductivity may be low as 0.5 µs/cm.
Increase in silica content
of effluent water of the mixed bed is a
signal of exhaustion of strong anion
resin and increase of conductivity
means exhaustion of cat ion resin.
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Ion Exchange Problems
Excessive
Regeneration
Frequency.
Higher Operating
Costs.
Poor Treated water
Quality.
Insufficient Volume of
Treated Water
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Common Causes of Ion Exchange
System Problem
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Desalination Water Chemistry Variation
Mechanical Malfunction
Resin Fouling and Degradation
Variation and operating and Regeneration Procedure
Variation in Flow Demand
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Demineralizers are used to provide highly purified water to high pressure boilers as feed water make-up. This highly purified water is also used in a vast number of other processes; such as wash water for microchip manufacturing.
Uses of
Demineraliz
ation water
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