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

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

Figure 18-32. Pr<strong>ed</strong>ict<strong>ed</strong> vibration of three-stage centrifugal pump showing effect<br />

of seals.<br />

the seal effects shift<strong>ed</strong> the critical spe<strong>ed</strong> from 1,800 to 3,700 rpm <strong>and</strong><br />

significantly increas<strong>ed</strong> the damping, which illustrates that the pump critical<br />

spe<strong>ed</strong> should be sensitive to seal stiffness effects. When the seals<br />

were consider<strong>ed</strong>, the pr<strong>ed</strong>ict<strong>ed</strong> amplitudes were r<strong>ed</strong>uc<strong>ed</strong> by a factor of<br />

more than 10 to 1.<br />

The vibrations on the pump were measur<strong>ed</strong> (Figure 18-33) using the<br />

peak-store capabilities of a real-time analyzer. The vibrations were low<br />

until the pump reach<strong>ed</strong> 3,300 rpm <strong>and</strong> then sharply increas<strong>ed</strong> to 6 mils<br />

peak-peak at 3,600 rpm. The design spe<strong>ed</strong> was 3,600 rpm; however, the<br />

pump could not run continuously at that spe<strong>ed</strong>. The pump spe<strong>ed</strong> was kept<br />

below 3,400 rpm so that the vibrations were less than 2 mils peak-peak.<br />

Even with the r<strong>ed</strong>uc<strong>ed</strong> pump spe<strong>ed</strong>, the pipe-laying barge was able to set<br />

pipe-laying records.<br />

After a year of operation, the pump vibrations began to increase until<br />

the vibrations at 3,400 rpm were unacceptable. The pressure breakdown<br />

bushing had worn which r<strong>ed</strong>uc<strong>ed</strong> its effective stiffness <strong>and</strong> the critical<br />

spe<strong>ed</strong> had dropp<strong>ed</strong> to 3,400 rpm. It was recommend<strong>ed</strong> that the pump be<br />

operat<strong>ed</strong> at a spe<strong>ed</strong> above the critical spe<strong>ed</strong>. This was tri<strong>ed</strong> <strong>and</strong> the pump<br />

operat<strong>ed</strong> at 3,600 rpm with vibration levels less than 2 mils peak-peak.<br />

The barge remain<strong>ed</strong> in service <strong>and</strong> reset the pipe-laying records during<br />

the next season.<br />

The data analysis technique us<strong>ed</strong> to determine this critical spe<strong>ed</strong> was to<br />

use the peak-store capabilities of the real-time analyzer. An alternate<br />

method would be to use a tracking filter to determine the critical spe<strong>ed</strong>

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