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

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164 <strong>Centrifugal</strong> <strong>Pumps</strong>: <strong>Design</strong> <strong>and</strong> <strong>Application</strong><br />

Figure 10-32. Performance of two half-capacity full head pumps install<strong>ed</strong> in parallel<br />

plott<strong>ed</strong> against system head curve.<br />

shar<strong>ed</strong> equally, <strong>and</strong> there is less chance of a pump operating at less than<br />

minimum continuous stable flow. Figure 10-32 shows our system curve<br />

<strong>and</strong> two half-capacity full head pumps install<strong>ed</strong> in parallel. In this particular<br />

system, parallel configuration is a poor choice. When only one<br />

pump is running, it is necessary to throttle to stay within operating range.<br />

Parallel configuration should be consider<strong>ed</strong> in systems where a substantial<br />

portion of the head is static. When pump configuration is not<br />

clear cut, it is wise to plot each station curve along with pump curves <strong>and</strong><br />

carefully analyze parallel versus series operation.<br />

Waterflood <strong>Pumps</strong><br />

Many types of pumps are us<strong>ed</strong> to extend the life of declining oil fields<br />

by injecting displacing fluids at pressures ranging from 2,OCX) psi to<br />

8,000 psi. In waterflooding applications (secondary recovery), centrifugals<br />

are preferr<strong>ed</strong> when injection capacities exce<strong>ed</strong> 10,000 BPD. Typical

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