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

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Pipeline, Waterflood <strong>and</strong> COa <strong>Pumps</strong> 163<br />

Figure 10-31. Performance of pump from Figure 10-30 in four-stage single<br />

pump operation <strong>and</strong> two pumps in series plott<strong>ed</strong> against system head curve<br />

To get 1,700 ft, we have two choices: The impellers of the 5-stage<br />

pumps can be trimm<strong>ed</strong> to about a 9 3 /4-in. diameter for 340 ft/stage. Alternatively,<br />

the pumps can be destag<strong>ed</strong> to 4 stages <strong>and</strong> at 425 ft/stage will<br />

not require impeller trimming. Refer to iso-curve (Figure 10-30) <strong>and</strong><br />

note how trimming affects efficiency at capacities approaching <strong>and</strong> beyond<br />

peak. At 1,319 GPM, destaging is obviously preferr<strong>ed</strong>. Figure 10-<br />

31 shows performance with one or two pumps operating.<br />

Series vs. Parallel<br />

A flat head-capacity curve is desirable for pipeline pumps install<strong>ed</strong> in<br />

series. When station capacity is being controll<strong>ed</strong> by throttling, less horsepower<br />

is lost than would be with a steep head-capacity curve. Capacity<br />

control of individual pumps does not present a problem since pumps operating<br />

in series will have the same flow rate.<br />

Where pipeline pumps are to be install<strong>ed</strong> in parallel, identical pumps<br />

with constantly rising head-capacity curves are usually call<strong>ed</strong> for. Load is

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