Page 441 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 7 .20          Lube, Seal and Control Oil System Best Practices


         Best
         Best
         Best Practice 7.20Practice 7.20Practice 7.20
         Continuously vent the non-operating cooler and filter by  Lessons Learned
         installing orificed return lines, and keep the transfer valve  Unit trips experienced during cooler and/or filter transfers
         bypass fill line opened to ensure warm-up of the cooler and  are usually blamedona ‘deadspot’ inthe transfervalvewhen
         filter prior to transfer, in cold climates, to prevent a unit  in fact, cool static oil of high viscosity in the non-operating
         shutdown on low oil pressure.                      cooler and/or filter caused the unit to trip on low oil pressure.
           In cold climates (ambient temperatures below 15 C at any time of  It should be noted that all types of transfer valves (six-way, ball

         the year), cool, static oil in the non-operating cooler and filter will cause  valve design, etc.) do not have a ‘dead spot’ that can cause an oil
         a transient pressure drop when it is changed on-line. This action can  system pressure drop when transferred.
         cause critical equipment unit trips on low oil pressure when the aux-
         iliary pump did not start, or did not start in time.  Benchmarks
           Requiring orificed vents on all coolers and filters, and keeping the
                                                            This best practice has been used since the mid-1990s, when unit trips
         non-operating vent lines open as well as the cooler and filter fill lines,  were experienced that were caused by a cooler and filter transfer to
         will ensure that non-operating coolers and filters are always maintained  cold, static oil. Since that time, all projects, with ambient temperatures
         at the same temperature as the operating vessels, and are vented and  below 15 C at any time of the year, have been required to have cooler

         ready for a successful transfer.                   and filter vents, and P&IDs indicating that valves were in open condi-
           Where a trip has been caused by the issue noted above, operating  tion. All field auxiliary system audits also recommended this approach
         procedures should be revised and orificed vents installed if required.  when ambient temperatures could fall below 15 C.




       B.P. 7.20. Supporting Material

       Transfer valves

       The function of the transfer valves in the auxiliary system are to
       allow transfer from one bank of components (coolers, filters,
       etc.) to the stand-by bank of components without significant
       pressure pulsations being introduced into the system. In addi-
       tion, transfer valves must be designed to positively shut off the
       unused components to allow for maintenance while the system
       is in operation.
          Types of transfer valves vary widely. Figure 7.20.1 shows
       a six-port transfer valve that allows flow into the valve to be
       diverted either to the left bank or right bank of components as
       shown in the standard schematic.
          Other types of transfer valves include the standard, globe-
       type valve shown in Figure 7.20.2.
          Both types exhibit the characteristic of minimal pressure
       change when transferring from one bank to the other. The six-
       ported valve should be designed with a lifting jack when a taper
       plug is used. This feature allows transfer of valves from one bank
       to another easily and still ensures tight shutoff of the valve when
       in its proper position.
          Selection of the valves should include material and sizing
       considerations. Materials of construction should be carbon steel
       as a minimum with stainless steel internals. The use of bronze
       components should not be considered in systems that can in-
       corporate gas entrained in the system fluid. In such systems
       brass, copper or bronze is not permitted. Valves are sized to
       match piping sizes in the system, which is normally designed for
       fluid velocities of four to six feet per second.


       Reliability considerations

       As previously mentioned, transfer valves including lifting jacks
       are susceptible to valve plug damage. Frequently, operators do  Fig 7.20.1   6 port transfer valve (Courtesy of Hycoa)

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