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

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Chemical <strong>Pumps</strong> Metallic <strong>and</strong> Nonmetallic 299<br />

pli<strong>ed</strong> with a glass or plastic bubble; glass is specifi<strong>ed</strong> in a refinery type of<br />

service.<br />

Shaft<br />

The shaft has to be design<strong>ed</strong> to take the radial, axial, cyclic, <strong>and</strong> torsional<br />

loads. The axial load, depending on suction pressure, can be in<br />

either direction. Shaft diameters are rat<strong>ed</strong> by horsepower per 100 RPM.<br />

The shaft material can be 1020, heat treat<strong>ed</strong> 4140 or 316. In each case the<br />

material should be review<strong>ed</strong> for impos<strong>ed</strong> stresses. Refer to Chapter 16<br />

for methods of calculations.<br />

impeller Attachment<br />

On chemical service pumps, impellers are usually attach<strong>ed</strong> with a male<br />

or female thread<strong>ed</strong> connection. Thread<strong>ed</strong> connections are us<strong>ed</strong> between<br />

the impeller <strong>and</strong> shaft because they can be more readily seal<strong>ed</strong> than when<br />

a key design is us<strong>ed</strong>, which inherently has an additional joint. Specifications<br />

do allow both types of connection.<br />

Bearings<br />

Specifications require that when the maximum hydraulic load from the<br />

largest impeller at a given spe<strong>ed</strong> is appli<strong>ed</strong> to the bearings, they will have<br />

a minimum L10 life of 17,500 hours. The designer <strong>and</strong> user should carefully<br />

select original or replacement bearings because the interchangeable<br />

dimensional envelope of an AFBMA bearing does not ensure that the size<br />

or number of balls are the same from one manufacturer to another,<br />

thereby resulting in a possible change in the rating of the bearing. It<br />

should also be remember<strong>ed</strong> that the life of a particular design will change<br />

with suction pressure.<br />

Most chemical pumps use semi-open impellers, <strong>and</strong> operate with a<br />

.010 to .020 inch gap between the impeller <strong>and</strong> casing wall. To maintain<br />

this clearance, the bearings should have .0015 to .002 of an inch axial<br />

input end play. Double-row bearings have an assembly end play of .002<br />

to .003 of an inch. Back-to-back bearings have an assembly end play of<br />

.005. However, the back-to-back bearings are more forgiving to misalignment<br />

when radial loads are appli<strong>ed</strong> to the bearings. The life of a<br />

back-to-back bearing is about twice that of the comparable double-row<br />

bearing. Back-to-back bearings are usually offer<strong>ed</strong> as an optional feature<br />

on chemical pumps. This applies to both horizontal <strong>and</strong> vertical pumps.

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