Page 500 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
P. 500

Pump Mechanical Seal Flush Best Practices  Be st Practice 8.2
              Seal fluid characteristics
                                                                       Orifice condition
              If all of the above mentioned items are in accordance with the  Seal gland condition
              seal design (EROE, seal chamber temperature and seal chamber  Throat bushing clearance
              pressure), a check of the seal fluid characteristics is required.  Cooler condition
                                                                       Strainer condition
              Figure 8.1.4 presents guidelines for checking the seal fluid
                                                                       Cyclone separator condition
              characteristics.
                                                                       Buffer fluid condition (tandem seal)
                                                                       Buffer fluid level (tandem seal)
                                                                       Pumping ring condition
                                                                       Buffer fluid pressure (tandem seal)
                  Take a sample to determine if debris is present
                  If seal fluid is not water or product fluid (which must meet
                  product specifications) have sample analyzed      Fig 8.1.5   Seal reliability as a function of flush system component
                  Send sample results to seal vendor               condition

              Fig 8.1.4   Seal fluid check guidelines
                                                                     Based on the seal flush plan used, the flush system compo-
                If the measured fluid sample parameters are not as stated on  nents should be checked in the logical order e starting with the
              the data sheet, consult with operations first to see if process  beginning of the flush system and ending with the throat bush-
              changes can be made. If process changes cannot be made, dis-  ing. (The exception is flush plan 13 which begins with the throat
              cuss this with the seal vendor representative.       bushing and ends at the pump suction pipe.) FAI ‘seal mainte-
                Variance in seal chamber pressures and temperatures, if the  nance best practice’ requires that the flush system be com-
              pump is operating in the EROE, will most likely be caused by  pletely checked (including the throat bushing clearance) each
              malfunction of components in the flush system. Figure 8.1.5  time a seal is changed. Note that this recommendation applies to
              defines those flush system components which can affect seal  all seal configurations: single, tandem (dual un-pressurized) or
              chamber pressures and temperatures.                  double (dual pressurized).







               Best Practice 8.2

               Pre-select mechanical seal and flush system design during    Flush line strainers
               the pre-FEED project phase, based on plant, company    Cyclone separators
               and/or industry experience, to optimize mechanical seal    Flush line coolers
               MTBF.                                                 Flush line strainers can expose plants to seal failure and safety
                  Use plant, company and industry lessons learned to properly select  issues, since they are not monitored in the control room and can result
               a flush system that will result in optimum seal life e in your plant!  in flush line blockage, which will fail the mechanical seal and can
                  Frequently, the flush system is selected by the process licensor or  expose the plant to significant safety issues in hydrocarbon
               the EP&C (contractor) and does not reflect actual plant conditions.  applications.
                  Be proactive early in the project design (pre-FEED phase) to con-
               vince project management of the proper flush systems to apply for all  Benchmarks
               pump services.
                                                                   This best practice has been used since the mid-1970s, when I became
                                                                   involved with pump selection. Since that time, prohibiting the use of
               Lessons Learned                                     flush line strainers and cyclone separators has resulted in optimum
               The use of the following flush system components where  mechanical seal safety and reliability during field mechanical seal
               they are not warranted has resulted in low mechanical seal  reliability optimization audits for all projects.
               MTBFs and has exposed plants to safety issues:



              B.P. 8.2. Supporting Material
                                                                    Mechanical seal flush must possess the following qualities for
                                                                    optimal seal life:
              Optimal seal plans for various applications             Cool
                                                                      Clean
                                                                      Approximately 345 kPa (50 psi) above vapor pressure (psia)
              We know the design aspects and how to monitor different flush
                                                                      Most importantly it must be cost effective!
              systems, but when would certain flush systems be better than
              others? Figure 8.2.1 lists the parameters required for a reliable
              flush source.                                         Fig 8.2.1   Optimal flush plans for various applications e overview
                                                                                                               471
   495   496   497   498   499   500   501   502   503   504   505