Page 546 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 9.5
                                                                    Dry Gas Seal Best Practices   Be st Practice 9.6


               Best
               Best Practice 9.5Practice 9.5
               Ensure that N 2 dew points are above L30 C(L22 F) to  Lessons Learned


               optimize the life of carbon used in seal faces and separa-  The use of ‘bone dry’ N 2 (dew points below L30 C) for in-

               tion seals.                                         termediate and separation sealing duties has resulted in
                  This is achieved by:                             low seal MTBFs (below 12 months).
                 Using small air separation units that produce moist N 2 (dew point >  In some cases, floating carbon seal wear was observed during the

                    30 C[ 22 F])                                   factory acceptance tests (FATs).

                 Using a N 2 bubbling system to condition ‘bone dry’ N 2 so that the


                  dew point >   30 C( 22 F)                        Benchmarks
                  Currently, air separation units produce nitrogen with dew points  This best practice was first used in 2008. Since that time, specifica-


               below  50 C( 58 F).                                 tions that require the dew point of supplied N 2 to be above  30 C

                  The life of carbon seals (radial and face seal) is significantly reduced in  ( 22 F) have been produced. It should be noted that small, dedicated




               dry gas applications where the N 2 dew points are below  30 C( 22 F).  N 2 generators can produce N 2 above  30 C( 22 F).

              B.P. 9.5. Supporting Material                        tioning is required whenever carbon stationary elements are
                                                                   used in either face or circumferential seals, when rubbing con-
                                                                   tact is anticipated for extended periods. For large steam or gas
              Seal gas conditioning                                turbine driven compressors that require slow roll for extended
                                                                   periods below the DGS lift-off speed, the best practice is to
              Cryogenic nitrogen (N 2 that has been liquefied) can damage the  condition the N 2 upstream of the coalescing filter system, raising
              carbon stationary faces during slow-speed operation e turning gear  its dew point to  30 C( 22 F), or higher.


              ratcheting or slow roll e when the faces are in contact. Cryogenic  Methods to increase N 2 dew point include mixing saturated
              N 2 is typicallyverydry,withadewpoint as lowas  90 C  nitrogen e from a bubbler chamber e with cryogenic nitrogen

              ( 130 F). But the self-lubricating quality of carbon is based on the  in an appropriate ratio, or mixing moist air with cryogenic ni-

              ability of its crystalline structure to adsorb and hold certain gases,  trogen, keeping the oxygen content below 5%. A dew-point
              including water vapor, which significantly reduce rubbing friction.  monitor and low-dew-point alarm are required for safe
                In the absence of water vapor, carbon has poor lubricating  operation.
              properties, and can wear rapidly. Therefore, dew point condi-



               Best
               Best Practice 9.6Practice 9.6Practice 9.6Practice 9.6Practice 9.6
               Best
               Best
               Best
               Always strongly recommend and justify the use of an ex-  Lessons Learned
               ternal source of clean, dry seal gas, if available, to elimi-  Seal gas conditioning does not ensure trouble free oper-
               nate the issues that will reduce seal system reliability.  ation in processes that cannot guarantee clean and dry
                  The main issues are as follows:                  seal gas. A clean, dry, external source of seal gas can be
                 Contamination of the seal by saturated gas        justified on the basis of lost revenue experienced in your
                 Contamination of the seal by process gas debris   plant, or through industry case histories that have not used
                 The necessity for a start-up gas                  a clean and dry external source of seal gas.
                 The necessity of a gas booster compressor system
                  During the early phases of the project (pre-FEED), discuss and in-  Benchmarks
               vestigate the viability and costs to use an external source of clean, dry  This approach has been used in all projects, and for seal gas system
               seal gas.                                           modification recommendations since the late 1990s. It has produced
                  If a continuous source of seal gas is available, the majority of issues  dry gas seal systems of the highest degree of safety and reliability (seal
               that affect the safety and reliability of the dry gas seal system will be  MTBFs > 70 months and compressor reliabilities > 99.7%).
               eliminated!


              B.P. 9.6. Supporting Material

              See B.P: 9.1 for supporting material.



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