Feedwater treatment, boiler water
conditioning and steam purity is important to be known. It is very important to
monitor and control boiler water chemistry to prevent failures due to
corrosion. The single largest cause of pressure part failures is waterside
corrosion.
The successful operation of steam
generating equipment depends upon a firm control of feed water and boiler water
to assure free from scale formation and corrosion due to water and steam in the
boiler.
Scale formation in boilers is
prevented by providing good make-up water to the feedwater system and by
avoiding condensate contamination. For higher pressure of boiler, the make-up
must be of condensate quality such as provided by evaporation or by demineralization.
Corrosion of metal surfaces in
contact with water and steam constitutes the major maintenance expense to the
power industry. The condensate and feed water must be free of dissolved
corrosive gases and the pH of the water must be properly adjusted to prevent
the attack of metal surfaces.
The oxygen content in the feed water
must be reduced to low levels by effective deaeration in the condenser and in
deaerating heaters. Care must be taken to prevent the introduction of air into
heater drips which may be added to the condensate. Make-up water from storage
tanks should not be added directly to the feed water system without deaeration.
Minimum forced boiler outage time has been realized where the oxygen content
has been reduced and held below 0.01 ppm. It is important to maintain a chemical
reducing environment in the boiler water and chemicals such as hydrazine have
been used effectively to achieve this.
Low pH feed water readily
dissolves iron and copper in the pre-boiler equipment. These corrosion products when introduced
into the boiler will contribute to the corrosion of boiler steam generating
surfaces. Oxides of iron and copper may permit the diffusion of boiler water to
the heated surfaces of the unit and cause locally high concentrations of boiler
water salines that result in the attack of the tube metal.
The pick-up of metals from
pre-boiler surfaces can be minimized by the addition of volatile alkaline
chemicals that raise the pH of the feed water. Ammonia or various amines, added
Lo maintain a pH range of 8.5 - 9.0 have produced the best results.
The philosophy of control of
boiler water pH varies widely. The caustic-based treatment, the coordinated
phosphate treatment and the volatile treatment have all been successfully
applied however the latter two methods of control are preferred in higher
pressure boilers.
For this boiler, the coordinated
phosphate treatment is adopted with using sodium-phosphate (Na3PO4) and
hydrazine (N2H4).
Recommended
Water Quality
The recommended limitation value of
feed water and boiler water is as follows:
Feed Water
|
Boiler
Water
|
||
pH at 25
degC
|
8.5 – 9.0
|
9.3 – 9.8
|
|
Hardness
(CaCO3)
|
ppm
|
0.0
|
-
|
Micro-Mhos/cm
at 25 degC
|
-
|
< 200
|
|
Dissolved
solids
|
ppm
|
-
|
< 100
|
Oxygen
|
ppm
|
< 0.007
|
-
|
Silica
|
ppm
|
-
|
< 1.5
|
Al
|
ppm
|
< 0.03
|
-
|
Fe
|
ppm
|
< 0.03
|
-
|
Cu
|
ppm
|
< 0.01
|
-
|
Hydrazine
(N2H4)
|
ppm
|
> 0.02
|
-
|
Phosphate
(PO4)
|
ppm
|
-
|
2 - 6
|
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