Page 225 - 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
              B.P. 3.23. Supporting Material                       Comparison of a liquid and gas
                                                                   sealing system
              The reliability of critical equipment is dependent on the
              reliability of each component in every auxiliary system that
                                                                   Figure 3.23.1 shows a liquid sealing system. Compare this
              is connected with it. How do we maximize critical equip-
              ment reliability? The easiest way is to eliminate the auxiliary  system to Figure 3.23.2, which shows a gas seal system, if the
              systems. Imagine the opportunity to eliminate all of the  same compressor were retrofitted for a gas seal. WOW e what
              components; pumps, filters, reservoirs, etc. and thereby in-  a difference. Why are there such a small number of components
              crease reliability and, hopefully, the safety of the equipment.  for the gas seal system? As an aid, refer to Figure 3.23.3, which
              The gas seal, as used in compressor applications, affords the  shows a typical pump liquid flush system as specified by the
              opportunity to achieve these objectives. However, the gas  American Petroleum Institute. This system incorporates a liquid
              seal is still part of a system and the entire gas seal system  mechanical seal and utilizes pump discharge liquid as a flush for
              must be properly specified, designed, maintained and oper-  the seal. Refer now to Figure 3.23.2 and observe the similarities.
              ated to achieve the objectives of optimum safety and re-  It should be evident that a gas seal system is simpler in com-
              liability of the critical equipment. In this chapter, the  pressor applications than a liquid seal system merely because the
                                                                   gas seal utilizes the process fluid. This is exactly the same case
              principles of gas seal design will be discussed and applied to
              various gas seal system types. In addition, best practices will  for a pump. By using the process fluid, and not a liquid, one can
                                                                   eliminate the need to separate liquid from a gas, thereby totally
              be discussed for saturated gas systems as well as shutdown
              philosophies.                                        eliminating the need for a liquid supply system and the need for
                                                                   a contaminated liquid (sour oil) drain system.
                                                                     Referring back to Figure 3.23.1, we can see that the following
                                                                   major components are eliminated:
              System function
                                                                   1. The seal oil reservoir
              The function of a gas seal system is naturally the same as a liquid  2. The pumping units
              seal system. The function of a fluid seal system, remembering  3. The exchangers
              that a fluid can be a liquid or a gas, is to continuously supply  4. The temperature control valves
              clean fluid to each specified seal interface point at the required  5. The overhead tank
              differential pressure, temperature, and flow rate. Therefore, one  6. The drain pot
              would expect the design of a gas seal and a liquid seal to be very  7. The degassing tank
              similar, which, in fact, they are. Then why are their systems so  8. All control valves
              different?                                           9. A significant amount of instrumentation





                       NOTE                                            GAS REF.UNE                   BUFFER
                       LEVEL IN OH TANK IS                   OH                                       GAS
                       MAINTAINED APPROX 10°                TANK        S.O. SUPPLY
                       ABOVE CENTRIFUGAL OF             LT
                                                                     PI
                       COMPRESSOR SHAFT                                                                LAEY
                                                                    ATMOSPHERIC                        SEAL
                                                                      BUSHING
                                            TI
                                                                           CONFAL SHIFT
                                                                                                     PROC. GAS
                               FILT                 FILT
                                                                                              GAS SIDE
                                                                      FLOW THROUGH
                               PDI                  PDI                   OIL                  SUMH     VENT
                                            TRANS. VALVE                                  VENT    DEVASTER   GAUGE
                               (S)                   (S)                                   SOUR  OIL
                           TCV                         TCV                     LCV
                                                                                                           LEVEL
                                                                                                   DPANER
                                                                                                    POT
                                                                          TANK
                           EXCHANGER              EXCHANGER             DEGASER
                                                                                                 MANWAVENT

                                                                                      SO RESERVOIR
                                                                                                         LEVEL
                                                                                                        GAUGE
                                                   M
                                  T                                        TI
                          MAIN PUMP              ALDC PUMP                      NORMAL LEVEL
                                                                                                        HEATER
              Fig 3.23.1   Typical seal oil system for clearance bushing seal (Courtesy of M.E. Crane, Consultant)

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