Page 414 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Lube, Seal and Control Oil System Best Practices  Best Practice 7 .13
              B.P. 7.13. Supporting Material                       components must have response times of the order of milli-
                                                                   seconds. When one considers the function of an auxiliary system
              Referring to the general definition of an auxiliary system which  and the fact that the slowest of critical equipment units operate
                                                                   at approximately 60 revolutions per second (3,600 RPM), the
              is ‘to continuously supply cool, clean fluid to each specified point
              at the required pressure, temperature and flow rate’, we can see  necessity of rapid system response time can be appreciated. If
              that the controls and instruments play a major role in the re-  the controls cannot respond to a transient response, the in-
              liability of auxiliary systems. The function of the controls and  strumentation and the critical equipment shutdown system
              instrumentation is to continuously supply fluid to each specified  (circuit breaker, steam turbine trip valve system, etc.) must
              point at the required pressure, temperature and flow rate. While  operate on demand to stop equipment operation. If the system
              it is true that pumps and coolers must be present, system con-  controls and instrumentation do not have sufficient response
              trols modify the operational characteristics of these components  times, a system liquid supply source (accumulator) is required
              to achieve the desired results. In addition, system in-  to provide flow during transient conditions. Using our system as
              strumentation initiates transient system response, continuously  an example, 60 GPM e or one gallon per second e are supplied
              monitors operation and shuts down critical equipment in the  to the unit. Suppose the main pump trips, and the normal flow
              event of an auxiliary system malfunction. In this section, we will  to the equipment is not reached for three seconds (until the
              examine important concepts that are at the heart of auxiliary  stand-by pump is at full speed and flow rate). An accumulator
              system reliability, define the function of major control and in-  with a liquid capacity of three gallons would enable the system
              strumentation components and discuss items that can signifi-  to function normally during the upset since it would supply the
              cantly reduce auxiliary system reliability.          required flow of one gallon per second. Note an accumulator size
                                                                   greater than three gallons would be required. This will be cov-
                                                                   ered separately.
              Types

              Types of major auxiliary system controls and instrumentation  Concepts
              are outlined in Figure 7.13.1. Note that types are defined by
              function. As an example, a positive displacement pump system  The use of concepts can be helpful in understanding the func-
              flow control consists of a pressure control valve that bypasses  tion of auxiliary system components and systems. In this section
              excess flow from the pump back to the system reservoir to  we will discuss:
              maintain a set system pressure. The function of this component,
              however, is to continuously supply the required flow of fluid to  - An equivalent orifice
              the system under varying system pressure drops and critical  - Sub-systems
              equipment component conditions (worn bearing, seal, etc.).  - An equivalent vessel
                                                                   - Control valve liquid coefficient e C v
                                                                   - A flow meter in every system
                                        Instrumentation monitor and
               Controls                 alarm                      The concept of an equivalent orifice
                  Positive displacement pump  System reservoir level  Bearings seals, etc. can be reduced to the concept of an
                  system flow control      Pump operation           equivalent orifice (see Figure 7.13.2). The equation for orifice
                  Dynamic pump system flow  System pressure         flow is:
                  control                 System temperature
                  Stand-by pump automatic start  Filter differential pressure                   2 r ffiffiffiffiffiffiffiffiffiffi
                                                                                                   Dp
                  Cooler temperature control  System differential pressure        Q ¼ C   C   D    S:G:
                                                                                           f
                  System differential supply  (variable reference pressure)
                  pressure control (constant  Variable speed pump driver  From the above equation it can be seen that flow to any
                                                                                                            2
                  reference pressure)     speed indicator          component is the function of the dimension ‘D ’ and 6P
                  System differential supply                       across that component. System components essentially
                  pressure control (variable
                                                                   experience two types of flow changes; the gradual flow change
                  reference pressure)                                                          2
                                                                   due to component wear (i.e., D change as in the case of
                                                                   bearing wear) or the sudden flow change due to a pressure
                                                                   change in the system. As can be seen from the above equation,
              Fig 7.13.1   Major auxiliary system controls and instrumentation (by  a sudden change of pressure as in the case of a hunting control
              function)                                            valve, or a sudden pressure spike due to component starting or
                                                                   stopping, will cause a corresponding sudden change in flow rate
                All system controls and instrumentation must function per-  to the component. Considering the speeds involved in critical
              fectly under both steady state and transient conditions. Under  equipment, one can appreciate that a short term, transient flow
              normal operation, a steady state control mode is approached  change can lead to significant component damage of the critical
              since flows, pressures and temperatures change very slowly if at  equipment (bearing, seals, etc.). The concept of reducing each
              all. While this mode of operation may appear to be ideal, it can  individual critical equipment component (bearing, seals, ori-
              be dangerous since control valves and instrumentation can bind  fices, etc.) to an equivalent orifice helps enormously in con-
              up due to debris and lack of movement. In transient mode,  ceptualizing transient system reactions.

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