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12.4.1.1 Check water inlet valve
Check water inlet valve for proper operation. Water supply pressures differing from
those originally specified will result in inadequate or erratic supply. Remedy by using a
properly sized valve or adjusted water supply pressure.
12.4.1 2 Sudden slugs of water
Sudden slugs of water will cause severe variations in steam pressure. These can be the
result of large volume returns from a condensate pump, or an oversized water inlet
valve. Inlet water flows should be as smooth as possible to avoid sudden steam
pressure drops, which will cause flashing and cavitation in the boiler feed pumps.
12.4.1.3 Water flows
Make certain that total water flows (returns and make-up) do not exceed rated
deaerator capacity.
12.5 Pumps
Unusual noise may be caused by several factors, as follows:
12.5.1 Cavitation
At any given temperature, all liquids have a definite pressure at which they will boil. It
follows, therefore, that a liquid will boil at any temperature, if the pressure is reduced
sufficiently. All pumps have a specific net positive suction heat (NPSH) requirement. If
this positive head is not available, pump cavitation will develop, resulting in severe
damage.
The required NPSH has been provided in this system, including additional height to
overcome suction line friction losses.
Suction piping is intentionally oversized to further reduce these losses.
Any unusual restriction, such as a clogged strainer, in the suction piping will cause
cavitation. The existence of such an obstruction can best be determined by a thorough
visual check or by installing a compound gauge (reading in vacuum and pressure) in the
pump suction line close to the pump. A thoroughly clean unrestricted line will produce
a pressure reading on the gauge, while the pump is running, equal to the operating
pressure of the deaerator plus the static head available. This head is measured in feet
from the water level to the pump suction centerline and converted to PSIG by dividing
by 2.31. A slight variance may be observed due to friction losses in suction piping. Any
restriction must be corrected immediately or severe pump damage will result.
The required NPSH has been provided in this system, including additional height to
overcome suction line friction losses.
Suction piping is intentionally oversized to further reduce these losses.
Any unusual restriction, such as a clogged strainer, in the suction piping will cause
cavitation. The existence of such an obstruction can best be determined by a thorough
visual check or by installing a compound gauge (reading in vacuum and pressure) in the
pump suction line close to the pump. A thoroughly clean unrestricted line will produce
a pressure reading on the gauge, while the pump is running, equal to the operating
pressure of the deaerator plus the static head available. This head is measured in feet