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

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

Figure 17-35. Package gas seal (courtesy of John Crane).<br />

A bushing is us<strong>ed</strong> at the bottom of the box, <strong>and</strong> the seal chamber at the<br />

inboard seal is essentially dead end<strong>ed</strong>. The only flow of hydrocarbon gas<br />

in this area is due to the leakage across the inboard seal face. Normal leak<br />

rates are in the range of 1.5 scfm. The space between the seal is vent<strong>ed</strong> to<br />

a flair or burn<strong>ed</strong> as fuel. The outboard seal prevents the gas from escaping<br />

to atmosphere. Since this is a non-contacting seal the life of the seal<br />

will not be affect<strong>ed</strong> by wear.<br />

Some applications still require double seals to provide a good running<br />

environment for the seal. Figure 17-36 shows a solution to sealing high<br />

pressure liquid carbon dioxide service. These seals are us<strong>ed</strong> on pumping<br />

equipment us<strong>ed</strong> to inject the liquid carbon dioxide into the ground for<br />

crude oil extraction. On this application, oil is circulat<strong>ed</strong> through the seal<br />

chamber at a pressure 10% greater than the pressure at the inboard seal<br />

from the liquid carbon dioxide. This seal is operating at the following<br />

conditions.<br />

• Liquid seal<strong>ed</strong>: carbon dioxide<br />

• Buffer liquid: oil<br />

• Stuffing box pressure: 2400 psig<br />

• Temperature: 65 °F<br />

• Specific gravity: 0.76 (oil)<br />

• Spe<strong>ed</strong>: 3550 rpm<br />

• Seal size: 3.750 inches

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