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

Pipeline, Waterflood and CO 2 Pumps 141
Figure 10-2. Specific speed describes impeller shape.
These losses can be generally classified as hydrodynamic, mechanical,
ring leakage, and disc friction. Analysis of these losses for one specific
performance at various speeds is shown in Figure 10-1. Pump efficiency
is a result of the sum of these losses and is influenced by specific speed,
which is basically a non-dimensional number. As discussed in Chapter 2,
the physical meaning of specific speed has no practical value; however, it
is an excellent means of modeling similar pumps and describes the shape
of the impeller under discussion (Figure 10-2).
Pump efficiency is also influenced by hydrodynamic size (Figure
10-3). For any given speed, pump efficiency increases with size of pump
or with hydrodynamic size (Figure 10-4). Through careful selection of
pump speed and stage number, optimum specific speed and hydrodynamic
size can be determined fo j r maximum efficiency.
Condition Changes
Many pipeline conditions require low-capacity, low-pressure start-up
with ultimate change over to high-capacity, high-pressure. By considering
this requirement at the design stage, pumps can be built to accommodate
the initial and ultimate conditions through field modifications. One
method is to adjust the ratio of liquid velocity leaving the impeller to liq-