Page 534 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Dry Gas Seal Best Practices   Be st Practice 9.1
              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 asuitablesep-
              aration seal must be provided to eliminate the possibility of oil  Dry gas seal design
              ingestion from the bearings. Whenever a gas seal system is
              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 sep-  The intention of this sub-section is to present the principles of
              aration between the liquid (lube) and gas seal system.  operation of a dry gas seal in a conceptual form. The reader is
                ‘O’ ring (secondary seal components) design and maintenance e  directed to any of the good literature available on this subject for
              most seal vendors state that ‘O’ ring life is limited, and they  a detailed review of gas seal design.
              should be changed every five years for operating seals as well as  Refer to Figure 9.1.5, which shows a mechanical seal used in
              spare seals. Experience has shown that dry gas ‘O’ ring seals can  pump applications, while Figure 9.1.6 shows a dry gas me-
              exceed this limit. It is recommended that seal vendors be  chanical seal utilized for compressor applications. The seal
              required to provide references for similar applications prior to  designs appear to be almost identical. Close attention to
              making a decision to change out the seals after five years.  Figure 9.1.6, however, will show reliefs of the rotating face of
                If all of the above considerations are incorporated in the  the seal.
              design of a gas seal system, its reliability has the potential to  Considering that both seals operate on a fluid may give some
              exceed that of a liquid seal system and the operating costs can be  hint as to why the designs are so very similar. The objective of
              reduced.                                             seal design is to positively minimize leakage while removing
                Before moving to the next section, however, one must con-  frictional heat, in order to obtain reliable, continuous operation
              sider that the relative reliability of gas and liquid seal systems is  of the seal. In a liquid application, the heat is removed by the
              a function of proper specification, design, etc. as mentioned  fluid which passes between the rotating and stationary faces and
              previously. A properly designed liquid seal system that is oper-  the seal flush and changes from a liquid to gaseous state (heat of
              ated and maintained can achieve reliabilities comparable to a gas  vaporization). This is precisely why all seals are said to leak and
              seal system. Also, when one considers the operating costs of the  explains the recent movement in the industry to seal-less pumps
              two systems, various factors must be considered. While the loss  in toxic or flammable service. If the fluid between the rotating
              of costly seal oil is positively eliminated, with a gas seal system  faces now becomes a gas, its capacity to absorb frictional heat is
              (assuming oil ingestion from the lube system does not occur) the  significantly less than that of a liquid. Therefore an ‘equivalent
              loss of process gas, while minimal, can be expensive. It is argued  orifice’ must continuously exist between the faces to reduce
              that the loss of process gas from a liquid seal system through  friction and allow a sufficient amount of fluid to pass and thus
              drainer and degassing tank vents is also significant. While this  take away the heat. The problem obviously is how to obtain this
              may be true in many cases, a properly specified, designed and  ‘equivalent orifice’. There are many different designs of gas
              operated liquid seal system can minimize process gas leakage  seals. However, regardless of the design, the dynamic action of
              such that it is equal or even less than that of a gas seal.  the rotating face must create a dynamic opening force that will
                There is no question that gas seal systems contain far fewer  overcome the static closing forces acting on the seal to create an
              components and are easier to maintain than liquid seal systems.  opening and hence ‘equivalent orifice’.
              These systems will be used extensively in the years ahead. The  Refer to Figure 9.1.7 which shows a typical gas dry seal face.
              intention of this discussion is to point out that existing liquid seal  Notice the spiral grooves in this picture; they are typically
              systems which cannot be justified for retrofit, or cannot be  machined at a depth of 100e400 micro inches.


























              Fig 9.1.5   Typical pump single mechanical seal

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