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

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Pipeline, Waterfiood and CO 2 Pumps 14? Figure 10-8. Performance range by volute chipping, impeller underfiiing, and installation of high-capacity impeller. Figure 10-9. Volute inserts convert high-capacity pump to low capacity.

148 Centrifugal Pumps: Design and Application Figure 10-10. Volute inserts. Bi-rotors Unusual pipeline requirements can often be satisfied using bi-rotor pumps. These are basically two single-stage pumps on the same shaft, with two conventional incoming and outgoing nozzles at each body cavity. Originally developed with double-suction impellers to reduce NPSHR at high flow rates, this design is extremely flexible. Two applications are now described. Bi-rotor pipeline pump. The pipeline conditions illustrated in Figure 10-15 have an ultimate pipeline capacity of 60,000 GPM requiring three pumps operating in parallel with each pump delivering 20,OCX) GPM at maximum pipeline pressure. During the early life of the pipeline, initial throughput would be 40,000 GPM. This would normally mean operating two pumps in parallel and throttling out excess pump pressure or reducing pump speed. A more economic approach would be to install a birotor pump with case construction that permits operation of the impellers either in series or in parallel. The conventional, integral cast cross-over

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

Figure 10-10. Volute inserts.<br />

Bi-rotors<br />

Unusual pipeline requirements can often be satisfi<strong>ed</strong> using bi-rotor<br />

pumps. These are basically two single-stage pumps on the same shaft,<br />

with two conventional incoming <strong>and</strong> outgoing nozzles at each body cavity.<br />

Originally develop<strong>ed</strong> with double-suction impellers to r<strong>ed</strong>uce<br />

NPSHR at high flow rates, this design is extremely flexible. Two applications<br />

are now describ<strong>ed</strong>.<br />

Bi-rotor pipeline pump. The pipeline conditions illustrat<strong>ed</strong> in Figure<br />

10-15 have an ultimate pipeline capacity of 60,000 GPM requiring three<br />

pumps operating in parallel with each pump delivering 20,OCX) GPM at<br />

maximum pipeline pressure. During the early life of the pipeline, initial<br />

throughput would be 40,000 GPM. This would normally mean operating<br />

two pumps in parallel <strong>and</strong> throttling out excess pump pressure or r<strong>ed</strong>ucing<br />

pump spe<strong>ed</strong>. A more economic approach would be to install a birotor<br />

pump with case construction that permits operation of the impellers<br />

either in series or in parallel. The conventional, integral cast cross-over

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