Page 523 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 8 .11          Pump Mechanical Seal Flush Best Practices
       B.P. 8.11. Supporting Material
                                                             Decreased Pump Flow:
       Seal vendors design the seal balance ratio and select face ma-  Increased P2
       terials based on a parameter known as the PV to be able to  Decreased P1
                                         3
       change the fluid to a vapor approximately / 4 of the way down  Decreased S.G.
       the seal faces (see Figure 8.11.1).                   Increased Pump Flow:
                                                                Decreased P2
                                                                Increased P1
                                                                Increased S.G.

                                                            Fig 8.11.3   Process effects on centrifugal pump flow


                                                              is designed to be at least 345 kpa (50 psi) or above the seal
                                                              fluid vapor pressure).
                                                            - The middle figure shows the desired design condition of
                                                                                                  3
                                                              changing the fluid to a vapor approximately / 4 of the way
                                                              down the faces. This is the design basis since it is known that
                                                              fluid characteristics, temperature and/or pressure will
                                                              change during operation a certain amount. Excessive changes
                                                              in any or all of these parameters will lead to seal failure.
                                                            - The last mode shows the case of no vaporization and
                                                              apparent seal failure. In reality, this is not a failure but only
       Fig 8.11.1   Mechanical seal primary face vaporization point
                                                              a seal fluid condition change that does not allow the seal fluid
                                                              to reach the fluid vapor pressure between the seal faces
                                                              before it exits the seal.
          As can be seen in Figure 8.11.2, head required is a function of
       the pressure differential across the pump flanges and inversely  As can be seen from Figure 8.11.1, the ability to achieve the
                                                                                 3
       proportional to the specific gravity of the pumped fluid.  objective of vaporization / 4 or 75% down the seal faces (see
       Therefore, process changes of P2, P1 and/or S.G. will change  center case in Figure 8.11.1) depends on the following:
       the pump flow in any centrifugal pump if a process control
       system is not present or operational (failed or in manual mode).  - Seal fluid characteristics e cleanliness, specific heat, vapor
                                                              pressure and viscosity
       These facts are presented in Figure 8.11.3.
          In Figure 8.11.1, three distinct operating modes are shown  - Pressure of the seal fluid in the seal chamber
       for the primary ring (on the left) and the mating ring (on the  - Temperature of the seal fluid entering the seal chamber
       right).                                                What determines the condition of items listed above? The

       - The top mode shows a condition of early vaporization which  process. Therefore, effective mechanical seal condition moni-
          can occur on light fluids, or hot fluids or where seal chamber  toring requires that all seal process conditions, as noted above
          pressure is lower than designed (note: seal chamber pressure  are considered.





                                                                  Fig 8.11.2   Head required by lower density fluid
























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