Boiler water treatment

Alkalinity

Graph of corrosion and pH

Treatment

For pressures below 20 bar dissolved O2 in the feed does not cause any serious problems so long as the water is kept alkaline
However cold feed should be avoided as this introduces large amounts of dissolved O2 are present, for pressures greater than 18.5 bar a dearator is recommended

Feed Treatment Chemicals

Sodium Hydroxide
Calcium Bicarbonate (CaCO3 + Na2CO3)
Magnesium Bicarbonate
Magnesium Chloride.
..
Sodium Phosphate
Calcium Carbonate
Calcium Sulphate
Magnesium Sulphate
All in this column precipitated as hydroxide or phosphate based sludges All in this column form sodium salts which remain in solution

Chemicals are normally added as a dilute solution fed by a proportioning pump or by injection from pressure pot.
Use of chemicals should be kept to a minimum.

Injection over a long period is preferable as this prevents foaming.

Excessive use of phosphates without blowdown can produce deposits of phosphides on a par with scale formations.

Therefore it is necessary to add sludge conditioners particularly in the forms of polyelectrolytes, particularly in LP blrs

Oxygen Scavengers

Polymer Treatment

Polymer is a giant molecular built up by stringing together simple molecules

E.G.
Polyelectrolytes-Formed from natural or synthetic ionic monomers
Polyacrylates - Polymers of acrylic acid
Polyamides - Polymers of amides

Polymer treatment prevents scale formation and minimises sludge formation. It can also loosen scale so established blrs introduced to this form of treatment may develop leaks where previously plugged with scale. Especially in way of expanded joints. Also can absorb trace oil

Use limited to LP blrs as no PO4 present to prevent caustic alkalinity

For auxiliary blrs this is a superior form of treatment to the old alkaline and phosphate treatment. The correct level of alkalinity must be maintained as too low a level neutralises the electric charge of the polyelectrolyte. Too high causes caustic alkalinity.

Amine treatment

Compounds containing nitrogen and hydrogen.

Neutralising amines

Hydrazine N2H4

see above

Bramine ( cyclohexalamine )

(Bull & Roberts amine treatment)

Neutralising amine as with hydrazine. Used with hydrazine to maintain feed water alkalinity within parameters. As a knock on effect will slightly increase boiler water alkalinity.

Stable at high temperatures so is used more than hydrazine to control the steam line alkalinity as there is less chance of copper corrosion which occurs with the prescience of ammonia

Proper boiler water treatment eliminates sludge and scale deposits within the boiler. However, over along period of time a film of copper and iron oxides build up on the tube surface. Most of these oxides are transported from oxides of corrosion within the feed system to the boiler with the condensate.

Bramine reduces this corrosion and eliminates the build up of these oxide deposits.

Mechanism of function
Condensate from the condenser is very pure and slightly acidic, often referred to as 'hungry water'. It can dissolve metals in trace amounts to satisfy this hunger.
Distilled make up water aggravates this situation containing much dissolved CO2 and hence being acidic carries its own corrosion products.
Trace amounts of bramine are introduced into the system to establish an alkalinity level greatly reducing the effects of the hungry water.

Some of the bramine is used almost immediately, most however, passes on to the boiler where it is then transported through boiler water, boiler stm drum, stm lines back to the condenser. It has no effect anywhere except the condensate system.

Bramine also has a cleaning effect and may assist in the cleaning the film off the tube over a period of time.
Bramine is safer to handle than Bramine and will protect all metals.

Hydrazine however readily breaks down to form ammonia which whilst protecting ferrous metals will attack those containing copper

Filming amines

Shows neutralising tendencies, main function however is to coat piping with a molecular water repellent protective film

Injection of amines
May be injected between HP and LP turbines in the X-over pipe or after the dearator.
Adding in X-over pipe-reduces corrosion of copper alloys
Dearator only effective as a feed heater

Adding after dearator -Dearator correctly performing as a dearator and feed heater. If possible the best system is to have a changeover to allow norm inj into the X-over at sea and injection after the dearator when the turbine shut down

Limits of density/pressure

Boiler presure/ chemical limits graph

Sludge conditioning agents

Treatment in boilers (non congruent)

LP tank blrs (<14 bar)

Na2CO3- precipitates salts, provides alkalinity
MgSO4- Sludge conditioners

Na2CO3 can break down to form NaOH in higher rated boilers hence initial dose with Na2SO4

Medium pressure tank blrs (<17.5 bar)

Na2CO3(3) + sodium phosphate(4) + sludge conditioners(1)

Medium to High pressure water tube <60 bar

Na2CO3 + Na2HPO4 +sludge conditioners

Oxygen scavengers also used to allow magnetite (Fe3O4) layer to form in the boiler

Boiler operating above 42 bar require a dearator.

HP to UHP blrs (42 to 80 bar)

Due to level of decomposition of Na2CO3 . NaOH preferred for better controllability Na2HPO4

NaOH attacks the magnetite layer. Congruent treatment used.

Permissible limits

ShellWTWTWTWTWT
TEST>PPM<17.5b<17,5b<32b<42b<60b<85b
HardnessCaCO3<=5<=5<=5<=1<=1<=1
P.alkCaCO3150-300150-300150-300100-15050-10050-80
T.D.S.CaCO3<=7000<=1000<=1000<=500<=500<=300
ClCaCO3<=1000<=300<=150<=100<=50<=30
PO4PO430-7030-7030-7030-5030-5020-30
N2H4N2H4------0.1 -1.00.1 - 1.0 0.1 - 1.0
SO3SO350-10050-10050-10020-50----
SiO2SiO2----------<=6.0
FeFe----------<=0.05
CuCu----------<=0.02
pHpH 10.5-11 10.5-11 10.5-11 10.5-11 10.5-11 10.3-11
Limits for feed water
ClCL<=10 <=5 <=1.0 <=1.0 <=1.0 <=1.0
O2O2---- ---- <=0.006 <=0.003 <=0.015 <=0.01
NH3NH3 ---- ---- ---- ----- ----- <=0.5
FeFe ---- ---- ---- ----- <=0.01 <=0.01
CuCu ---- ---- ---- ----- <=0.01 <=0.01
pHpH ---- ---- ---- 8.5-9.2 8.5-9.2 8.5-9.2