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Centrifugal Pumps Design and Application 2nd ed - Val S. Lobanoff, Robert R. Ross (Butterworth-Heinemann, 1992)

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Vertical <strong>Pumps</strong> 129<br />

Condensate <strong>and</strong> Heater Drain <strong>Pumps</strong><br />

This pump type is typically install<strong>ed</strong> as two 50% capacity pumps taking<br />

suction from a header connect<strong>ed</strong> to a condenser or heater for boiler<br />

fe<strong>ed</strong> water. The available NPSH is normally only two to four feet at the<br />

mounting floor, requiring additional NPSH to be built into the barrel.<br />

The multi-stage bowl assembly, typically in the 1,500 to 2,500 specific<br />

spe<strong>ed</strong> range, can be fitt<strong>ed</strong> with a special first-stage impeller to meet the<br />

requir<strong>ed</strong> NPSH. Figure 9-13 shows a unit with a double suction firststage<br />

impeller. The suction nozzle may be locat<strong>ed</strong> either in the barrel or<br />

the discharge head, whichever the user prefers. The shaft seal in the discharge<br />

head is typically of the mechanical face type <strong>and</strong> must be water<br />

quench<strong>ed</strong> because the seal is under vacuum when on st<strong>and</strong>by. A continuous<br />

vent line must be provid<strong>ed</strong> from the top of suction side in the pump to<br />

the vapor phase in the suction tank (condenser). A minimum flow bypass<br />

line may be requir<strong>ed</strong> at the discharge control valve if extend<strong>ed</strong> low flow<br />

operation cannot be avoid<strong>ed</strong>. Induction motor drive is the most common,<br />

but a variable spe<strong>ed</strong> drive offers advantages for peak load<strong>ed</strong> plants. Cotidensate<br />

pumps normally operate in the 130°F range, <strong>and</strong> cast iron bowls<br />

with bronze impellers <strong>and</strong> bearings are usually adequate. For applications<br />

where the peripheral vane velocity in the suction eye exce<strong>ed</strong>s 80<br />

feet per second, a stainless steel impeller should be us<strong>ed</strong>. Some users will<br />

not permit bronze materials in the system because it may contribute to<br />

corrosive attack on condenser tube welds. In these cases, all impellers<br />

should be furnish<strong>ed</strong> in martensitic steel. Heater drain pumps may operate<br />

up to 350°F <strong>and</strong> require impellers of martensitic steel <strong>and</strong> bearings of a<br />

carbon-graphite composite. Because flashing in the first stage cannot always<br />

be avoid<strong>ed</strong> in this service, injecting second-stage pump pressure<br />

into the suction case bearing is recommend<strong>ed</strong>.<br />

Process <strong>Pumps</strong><br />

These pumps are of multi-stage construction, with a special first-stage<br />

impeller to meet the limit<strong>ed</strong> available NPSH. H<strong>and</strong>ling liquids near their<br />

boiling point requires a continuous vent line from the pump suction side<br />

back to the suction source. The mechanical shaft seal can either be<br />

mount<strong>ed</strong> internally in the discharge stream, flush<strong>ed</strong> <strong>and</strong> cool<strong>ed</strong> by the<br />

pump<strong>ed</strong> liquid, or mount<strong>ed</strong> in an external, water jacket<strong>ed</strong> stuffing box<br />

for high temperature applications. Materials for the bowl assembly <strong>and</strong><br />

fabricat<strong>ed</strong> components are select<strong>ed</strong> to suit the liquids h<strong>and</strong>l<strong>ed</strong>, including<br />

cavitation resistant material for the first-stage impeller, when applicable.

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