Page 579 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 1 0.9          The Post-Shipment Phase: Installation, Pre-Commissioning, Commissioning and Start-up Best Practices

        Table 10.8.2 Lube system check list (example)dCont'd
        Item      Description                                  Specified value             Actual value Witnessed by

        30.       Stop aux. pump motor and observe:
                  A. All control valves remain stable.                                    _____
                  B. Min. press. spike on P.I. lube            90 Kpa T&T valve does not trip  _____
                  P.I. Control                                                            _____
                  PDI LP Case DP                               207 Kpa                    _____
                  PDI LP Case DP                               207 Kpa                    _____

        31.       With turbine operating. Bleed press, from PSL and observe aux. pump     _____
                  starts and that all valves remain stable.
        32.       Having satisfactorily completed all items above, secure both aux. and   _____
                  main pump and sign off as being acceptable for operation.
                  NOTE: At this point, elect one driver and continue to operate the
                  console 24 hours a day.
        NOTE 1    RVs will continuously pass a small stream of oil. Actual setting will be
                  that pressure at which stream volume increases. Observe by un-
                  bolting FLGS at reservoir. Accumulation value is with pump discharge
                  block fully closed.
        NOTE 2    Block out gas signal to diff. control valve during this step.










         Best Practice 10.9Practice 10.9Practice 10.9
         Best
         Best
         Perform critical compressor air or nitrogen runs during  Lessons Learned
         pre-commissioning to confirm that all phases of con-  Failure to include an air or inert gas run in pre-commis-
         struction have been successfully completed.        sioning exposes the plant to reduced safety and reliability.
           The following phases should be checked:            Whenever the project team was able to justify an air or inert gas run
           Preservation                                     prior to plant start-up, items were identified that would have impacted
           Foundation preparation                           the safety and reliability of the critical equipment train up to the first
           Grouting                                         turnaround.
           Soft foot check
           Process pipe connection                          Benchmarks
           Final alignment                                  This best practice has been recommended since 1985 to achieve plant
           Functional auxiliary system checks               start-ups with minimum delays and optimum plant safety and
                                                            reliability.
           The air or nitrogen run will ensure that the mechanical behavior of
         the critical machinery train matches that of the FAT (factory accep-
         tance test) mechanical test, thus confirming that all construction issues
         were properly addressed.






                                                              The test objective is to completely confirm the mechanical
       B.P. 10.9. Supporting Material                       operation of the machinery and the associated auxiliary systems
                                                            prior to plant operation.
       The site air or inert gas run procedure should be developed  Process piping may have to be disconnected for these runs to
       along with the machinery vendor to ensure that all opera-  prevent overheating. In some applications, temporary temper-
       tional differences (power requirements, dry gas seal condi-  ature measuring devices may have to be installed to curtail
       tions, pressures and temperatures, etc.) are considered and  testing when casing temperatures exceed design limits


       planned for.                                         (approximately 200 C [400 F]).
           550
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