Page 459 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 7 .29          Lube, Seal and Control Oil System Best Practices
       lubrication oil supply, even in the event of failure of the stand-by  and the bypass valve opens to control system pressure to
       pump.                                                a pre-set value, thereby bypassing excessive auxiliary pump
          Such a system is useful in areas where an alternative form of  (stand-by pump) flow. Upon starting of the critical equipment
       energy is not available for main and spare pumps, as on platforms  unit, the bypass valve will react to increasing main pump flow
       or in chemical plants where a utility steam system is not  and will gradually open to the point that it would be at maxi-
       installed.                                           mum stroke if the stand-by pump remained in operation. When
          However, the system must still be designed to effectively lu-  the stand-by pump is shut down, the response of the bypass
       bricate all bearings prior to the main pump attaining full flow rate  valve must be equal to the decrease of flow from the auxiliary
       (speed). To facilitate this, the auxiliary pump is designed to start  stand-by pump such that system pressure does not drop below
       before the main critical equipment driver is started (permissive  trip setting.
       arrangement), and either automatically or manually shut off once  Refer back to the concepts of an equivalent vessel and orifice
       the shaft-driven pump attains sufficient speed. On shutdown, the  discussed in previous sections. In this case, the supply to the
       reverse occurs e the auxiliary pump will start on deceleration of  equivalent vessel (from the auxiliary pump) instantaneously
       the main pump. The signal to start the auxiliary pump can be  drops while the demand from the critical equipment is constant
       critical equipment speed or system pressure. If a system is not  thus causing an instantaneous drop in equipment vessel pres-
       designed for automatic shutoff of the auxiliary pump, care must  sure. Prior to shutdown of the auxiliary pump, excessive supply
       be taken to ensure that it is designed for continuous two-pump  was recirculated by the bypass valve. Upon rapid decrease of
       operation. It is recommended that auxiliary pumps be shut off  supply flow, the bypass valve must decrease demand at the same
       during critical equipment main pump operation.       rate to ensure pressure in the system (equivalent vessel) is
          A particular concern with this system design is to ensure  maintained at a constant value. Failure to do this can result in
       priming of the main pump. Frequently, the main pump is at  critical equipment shutdown.
       a significant height above the fluid reservoir. In this case, care
       must be taken to ensure proper priming of main pump prior to  Main and auxiliary A.C. motor-driven pumps,
       start-up. Many systems incorporate a priming line from the
       auxiliary pump to fill the main pump suction line. This requires  D.C. motor-driven emergency pump
       a check valve (foot valve) in the main pump suction line and  Refer to Figure 7.29.2. This application would be used in fa-
       a self-venting device to ensure air is not entrained in the suction  cilities where steam systems are not available, such as chemical
       line of the main pump. Frequently, systems of this type do not  plants or in operations at remote locations or on offshore plat-
       incorporate a vent line and are susceptible to main pump cavi-  forms. In this case, both pumps (main and stand-by pump),
       tation on start-up.                                  would shut down in the event of a power failure. If the critical
          Referring to Figure 7.29.1, let’s examine the bypass valve  equipment unit is also motor driven, it too will cease operation.
       response in the event that the auxiliary pump does not shut off  The design objective of this auxiliary system is to provide
       after the shaft-driven pump has attained full flow (speed). Upon  a sufficient flow, via an emergency pump driven by a DC source
       initial auxiliary pump start-up, flow is supplied to the system  (direct current), for a sufficient time to promote the safe


































       Fig 7.29.2   Lube oil system, main pump shaft-driven (Courtesy of Elliott Co.)

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