WATER PROPERTIES SENSING

4- 7.1 Steam-Generator Feedwater Specifications

Feedwater conditioning is required to maintain opera­tional capability of the steam generator The steam­generating surfaces remain clean and heat-transfer capa­bilities are favorable if good water quality is maintained The minimum standards given in Table 4 19 should be maintained for satisfactory feedwater quality.

4- 7.2 Usual Impurities in Water Supply

Table 4.20 lists the impurities usually found in water supplies and indicates their properties, effects, and methods for treatment and removal.

4- 7.3 Effect of Impurities in Steam-Generator Feedwater

(a) Total Solids (Dissolved and Undissolved). The total solids in the feedwater is a general indicator of how much material is collecting in the steam generator. Insoluble materials are deposited on the steam-generator surfaces. The soluble material (e. g., NaCl, NaOH, and Na2S04) is carried over in the steam with the remaining material and tends to collect on the steam-generator tubes. The types of constituents in the feedwater depend on the preboiler characteristics. The quantity of soluble material should be larger than the quantity of insoluble material. Turbidity is a measure of the undissolved constituents, and electrical conductivity is a measure of the dissolved constituents

(b) Dissolved Oxygen. Dissolved oxygen promotes cor­rosion in the steam generator and therefore should be kept as low as possible. Deaeration removes much of the dissolved oxygen. Hydrazine, a good oxygen scavenger, can eliminate the remaining oxygen. A high level of dissolved

Maximum total solids (dissolved and suspended), ppb

50

Maximum dissolved oxygen, ppb

7

Maximum total silica (as Si02), ppb

20

Maximum total iron (as Fe), ppb

10

Maximum total copper (as Cu), ppb

2

pH at 77° F (adjusted with ammonia)

9 3 to 9.5

Total hardnesst

No specification

Organics$

listed

0

Lead§

0

*From Babcock and Wilcox Nuclear Power Generation Division, Water Chemistry Manual, Part 8, p 8-1

tHardness constituents should be eliminated because of deposition on steam generator surfaces

^Organic contamination can lead to resm fouling § Lead contamination should be kept below the lowest value detectable by acceptable methods to avoid problems with Inconel-600 in oxygenated water

oxygen could indicate a malfunctioning deaerator or an air leak in the area of the condenser.

(c) Total Silica. Silica should be maintained at a low level for two reasons (1) silica can concentrate in the steam generator and subsequently plate out on heat-exchange surfaces thereby reducing steam generation and (2) silica may carry over and plate out m the turbine causing turbine inefficiency. A higher than allowable silica concentration implies a demineralizer breakthrough. Switching to the spare demineralizer while the exhausted resin is regenerated or changed can probably eliminate the high silica level.

(d) Total Iron. Iron tends to build up in the steam generator and reduces its efficiency by degrading the heat-transfer characteristics. The level of iron in the feedwater affords some measure of the degree and rate of corrosion in the system.

(e) Total Copper. Copper should be avoided where possible in the feedwater system. Equipment in contact with the feedwater should be ferritic or austenitic stainless steel. Copper in the feedwater system can be carried into the steam generator in solution and plate out there. The copper plate can then make it necessary to clean the steam generator in a two-stage process one for copper and another for iron. Copper carryover in the steam can plate out on the turbine and lower its efficiency Copper alloy tubes in the condenser should be satisfactory because the temperatures and pressures are reduced and the dissolution of the copper is less likely.

(f) Total Lead. Lead in the feedwater concentrates in the steam generator This can result in problems with Inconel in oxygenated water containing lead Satisfactory instrumentation for monitoring traces of lead is not available at the present time

(g) Conductivity. Cation (positive-ion) conductivity cells can be used to monitor the feedwater Measurements

Impurity

Formula

Molec*

ular

weight

Equiv­

alent

weight

Solu­

bility

Probable effect in boiler

Methods of treatment and removal

Calcium bicarbonate

Ca(HC03)2

162 10

81.05

Moderate

Scale and sludge,

liberates C02

Calcium carbonate

CaC03

100.08

50.04

Slight

Scale and sludge,

liberates C02

Calcium hydroxide

Ca(OH),

74.10

37.05

Slight

Scale and sludge

Calcium sulfate

CaSO,

136.14

68.07

Moderate

Hard scale

Calcium silicate

Vanable

Slight

Hard scale

In external treatment of calcium

Calcium chloride

Cad,

110 99

55.50

Very solu-

Corrosive, scale

and magnesium compounds,

ble

and sludge

lime and soda softeners

Calcium nitrate

Ca(fJ03)2

164.10

82.05

Very solu-

Corrosive, scale

plus coagulation and filtration

ble

and sludge

give partial removal, Zeolite

Magnesium bi-

Mg(HC03)3

146.34

73.17

Moderate

Deposits, liberates

>

softeners and evaporators

carbonate

co2

give more complete removal,

Magnesium carbo-

MgC03

84.32

42.16

Slight

Deposits, liberates

the former replacing

nate

co3

calcium and magnesium with

Magnesium hydroxide

Mg(OH)3

58.34

29.17

Very slight

Deposits

sodium, corrosive compounds

Magnesium sulfate

MgSO,

120.38

60.17

Very solu-

Corrosive, deposits

require alkali treatment

ble

Magnesium silicate

Variable

Slight

Hard scale

Magnesium chloride

MgCl3

95.23

47.62

Very solu-

Corrosive,

ble

deposits

Magnesium nitrate

Mg(N03 )3

148 34

74.17

Very solu-

Corrosive, deposits

ble

Sodium bicarbonate

NaHC03

84.00

42.00

Very solu-

Increases alkalinity

ble

and soluble solids,

liberates C02

Sodium carbonate

Na2C03

106.00

5 3 00

Very solu-

Increases alkalinity

ble

and soluble solids,

Excess sodium alkalinity may

liberates C02

be reduced by boiler

Sodium hydroxide

NaOH

40.00

40.00

Very solu-

Increases alkalinity

blowdown, it sometimes

ble

and soluble solids

is neutralized with

Sodium sulfate

Na2 SO,

142 05

71.03

Very solu-

Inhibitor for

sulfuric acid externally,

ble

caustic embrit-

phosphoric acid and acid

tlement, in-

► phosphates also are used

creases soluble

evaporation is best

solids

practical means of re

Sodium silicate

Variable

Very solu-

Increases alkalinity,

moving sodium compounds

ble

may form

from feedwater, boiler

silica scale

blowdown is used for internal

Sodium chloride

NaCl

58 45

58 45

Very solu-

Increases soluble

reduction of soluble solids

ble

solids, en-

courages corrosion

Sodium nitrate

NaN03

85.01

85.01

Very solu-

Increases soluble

ble

solids

Iron oxide

Fe303

159 68

26.61

Slight

Deposits, en-

Coagulation and filtration,

courages corrosion

evaporation, blowdown

Alumina

A1303

101 94

16.99

Slight

May add to

Coagulation and filtration,

deposits

evaporation, blowdown

Silica

SiO,

60.06

30.03

Slight

Hard scale, acts

Precipitation with aluminates,

as binder for

coagulation and filtration,

deposits

evaporation, blowdown

Dissolved oxygen

o2

32.00

16.00

Slight

Corrosive

Deaeration preferred

Carbonic acid or

h2co3

62 02

31.01

Very solu-

Retards hydrolysis

Deaeration and alkali

dissolved C02

ble

of carbonates,

treatment

reduces alkalinity

Hydrogen sulfide

H2S

34 08

17 04

Very solu-

Corrosive

Deaeration and alkali treat-

ble

ment

Acids, organic and

Very solu

Corrosive

Neutralization by alkali treat-

mineral

ble

ment

Oil and grease

Slight

Corrosive, deposits,

Coagulation and filtration,

foaming and priming skimming

Organic matter

Very solu-

Corrosive, deposits,

Coagulation and filtration,

ble

foaming and

evaporation

priming

•From R. T. Kent, Mechanical Engineers’ Handbook, Power, 12th ed, p. 7 51, John Wiley & Sons, Inc, New York, 1950

Подпись: Fig. 4.42—pH vs. hydrogen-ion concentration. (From D. M. Considine, Process Instruments and Controls Handbook, p. 6-96, McGraw-Hill Book Company, Inc., New York, 1957.)

should be made after removal of the ammonia that is used to regulate the pH

(h) Corrosion. The principal accelerators of corrosion are dissolved oxygen, acids, surface deposits, especially those electronegative to steel, dissimilar metals in contact, and electrolytes.

Common methods to prevent corrosion are removal of dissolved gases, especially oxygen, neutralization of acids and maintenance of desirable alkalinity and pH, periodic mechanical cleaning, and avoiding excessive salt concentra­tions.