Page 483 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 7 .34          Lube, Seal and Control Oil System Best Practices


























































       Fig 7.34.12   Typical seal oil system (Courtesy of M.E. Crane, Consultant)

       maintaining the same 34.5 kPa (5 psi) differential, the upstream  Example 5: Trapped bushing gas side seal:
       pressure across the valve would be approximately 1,410 kPa (205  atmospheric side bushing seal with flowthrough
       psi) instead of 34.5 kPa (5 psi). Consequently, the valve position  design
       would change significantly, but still would have to control the
       differential accurately to maintain 34.5 kPa (5 psi). Reduction of  This system would follow exactly the same design as the system
       this pressure in any amount below 34.5 kPa (5 psi) could result in  described in Example 4. The only difference would be in the
       instantaneous bushing failure. However, if a level control valve  amount of flow registered in the seal oil drainer. A trapped
       were installed, the accuracy of the valve would be measured in  bushing system is designed to minimize seal oil drainer pot
       mm (inches) of oil instead of kPa (psi). Any level control system  leakage. Typical values can be less than 19 l/day (5 gal/day).
       could control the level within 50 mm (2"), which would be only
       a 0.4 kPad (0.06 psid) variation in pressure differential!  Seal supply system summary
          This example shows that the accurate means of controlling
       differential pressure for systems requiring control of small dif-  All of the above examples have dealt with a system incorporating
       ferential values, is to use level instead of differential control.  one seal assembly. It must be understood that most systems
       This system would be designed such that the combination of the  utilize two or more seal system assemblies. Typical multi-stage
       atmospheric flow and the through flow through the seal would  compressors contain two seal assemblies per compressor body
       be equal to the flow from the pump.                   and many applications contain upwards of three compressor

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