Page 227 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Compressor Best Practices   Best Practice 3 .23
              Considerations for system design                     exceed that of a liquid seal system, and the operating costs can
                                                                   be reduced.
              As mentioned above, there are disadvantages to a gas seal  Before moving to the next section, however, one must
              system; which are not insurmountable but must be considered  consider that relative reliability of gas and liquid seal systems
              in the design of such a system. These considerations are as  are a function of proper specification, design, etc. as mentioned
              follows:                                             previously. A properly designed liquid seal system, which is
                                                                   well operated and maintained, can achieve the reliabilities of
              Sensitivity to dirt e since clearances between seal faces are  a gas seal system. Also, when one considers the operating costs
              usually less than 0.0005 inch and seal design is essential to  of the two systems, various factors must be considered. While
              proper operation, the fluid passing between the faces must be  the loss of costly seal oil is eliminated, with a gas seal system
              clean (5e10 microns maximum particle size). If it is not the  (assuming oil ingestion from the lube system does not occur)
              small grooves (indentations) necessary for seal force separation  the loss of process gas, while minimal, can be expensive. It is
              will become plugged thus causing face contact and seal failure.  argued that the loss of process gas from a liquid seal system
                Sensitivity to saturated gas e saturated fluids increase the  through drainer vents and degassing tank vents is also signifi-
              probability of groove (indentation) blockage.        cant. While this may be true in many cases, a properly speci-
                Lift-off speed e as will be explained below, a minimum speed  fied, designed and operated liquid seal system can minimize
              is required for operation. Care must be taken in variable speed  process gas leakage such that it is equal or even less than that
              operation to ensure that operation is always above this speed. It  of a gas seal.
              is recommended that the seal test be conducted for a period at  There is no question that gas seal systems contain far fewer
              turning gear speed to confirm proper ‘lift off’ followed by seal  components and are easier to maintain than liquid seal systems.
              face inspection.                                     These systems will be used extensively in the years ahead. The
                Positive prevention of toxic gas leaks to atmosphere e since all  intention of this discussion is to point out that existing liquid seal
              seals leak, the system must be designed to preclude the  systems that cannot be justified for retrofit, or cannot be
              possibility of toxic of flammable gas leaks out of the system. This  retrofitted easily, can be modified to minimize outward gas
              will be discussed in detail below.                   leakage and optimize safety and reliability.
                Possible oil ingestion from the lube system e a suitable
              separation seal must be provided to eliminate the possibility of
              oil ingestion from the bearings. Whenever a gas seal system is  Dry gas seal design
              utilized, the design of the critical equipment by definition
              incorporates a separate lube oil and seal system. Consideration  Principles of operation
              must be given during the design or retrofit phases to the
              separation between the liquid (lube) and gas seal system.  The intention of this sub-section is to present a brief detail of the
                ‘O’ ring (secondary seal components) design and    principles of operation of a dry gas seal in a conceptual form. The
              maintenance e most seal vendors state that ‘O’ ring life is  reader is directed to any of the good literature available on this
                                                                   subject for a detailed review of gas seal design.
              limited and they should be changed every five years. This
                                                                     Refer to Figure 3.23.4, which shows a mechanical seal uti-
              applies to both operating and spare seals. My experience has  lized for pump applications, and Figure 3.23.5, which shows
              shown that dry gas ‘O’ ring seals can exceed this limit. It is
              recommended that seal vendors should provide references for  a dry gas mechanical seal utilized for a compressor application.
              similar applications prior to making a decision to change out the  The seal designs appear to be almost identical. Close attention to
              seals after five years.                               Figure 3.23.5, however, will show reliefs of the rotating face of
                                                                   the seal. Considering that both seals operate on a fluid may give
                If all of the above considerations are incorporated in the  some hint as to why the designs are very similar. The objective of
              design of a gas seal system, its reliability has the potential to  seal design is to positively minimize leakage while removing



                                                                                         Fig 3.23.4   Typical pump single
                                                                                         mechanical seal



















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