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

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

Casing Mismatch<br />

On horizontally split pump casings mismatching between the upper <strong>and</strong><br />

lower casing halves is quite common. This mismatch is normally correct<strong>ed</strong><br />

by h<strong>and</strong> filing using a template (Figure 6-7). The same template is<br />

us<strong>ed</strong> by the machine shop to define bolt locations <strong>and</strong> also by the foundry.<br />

It is quite important that the fluid passages in both halves of the casing<br />

match in both the horizontal <strong>and</strong> vertical planes since any mismatching<br />

will adversely affect pump performance.<br />

Check for Volute interference<br />

After the pump casing is completely finish<strong>ed</strong> to satisfy quality specification,<br />

the assembl<strong>ed</strong> rotating element should be install<strong>ed</strong> in the casing<br />

(as shown in Figure 6-8) to check for interference against volute walls.<br />

Also check the element for total end float, which should be no less than<br />

one-half inch total or one-quarter inch on each end.<br />

* It is important to have the volute symmetrical about shaft centeriine.<br />

* A Vie-in, deep relief should be machin<strong>ed</strong> around each stud at the split.<br />

At each stud at assembly the metal will rise. The relief will allow the<br />

gasket to lay flat, r<strong>ed</strong>uce gasket area, <strong>and</strong> increase gasket unit pressure.<br />

* It is very important to install splitters at each impeller suction entrance.<br />

These can be install<strong>ed</strong> recess<strong>ed</strong> at the casing split or cast on casing hub<br />

rings.<br />

« Horizontally split centrifugal pumps are design<strong>ed</strong> for relatively high<br />

pressures; 3,000 psi hydrotest is very much st<strong>and</strong>ard by many manufacturers.<br />

Pressure up to 6,000 psi hydro can be obtain<strong>ed</strong> by special<br />

design of bolting <strong>and</strong> case.<br />

It is essential (to prevent stage-to-stage bypassing) to have all bolts locat<strong>ed</strong><br />

as close as possible to the open area. The high pressure differential<br />

in oppos<strong>ed</strong> impeller design multi-stage pumps is between two center<br />

stages <strong>and</strong> at the high pressure end. Particular attention to bolting should<br />

be paid in these two areas. It is sometimes advantageous to provide elevat<strong>ed</strong><br />

bosses to bring bolting closer to open area.

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