Page 584 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
P. 584

The Post-Shipment Phase: Installation, Pre-Commissioning, Commissioning and Start-up Best Practices  Be st Practice 1 0.11
              Thrust bearings                                      Auxiliary systems
              Figures 10.11.9 and 10.11.10 show condition parameters and  Condition monitoring parameters and their alarm limits are
              their limits for anti-friction and hydrodynamic thrust bearings.  defined in Figures 10.11.12 and 10.11.13 for lube and pump
                                                                   flush systems.
              Seals                                                  Figures 10.11.14, 10.11.15 and 10.11.16 present condition
                                                                   monitoring parameters and limits for dynamic compressor per-
              Figure 10.11.11 presents condition parameters and their limits
              for a pump liquid mechanical seal.                   formance, liquid seals and seal oil systems.



                                                                    Lube oil systems
               Thrust bearing (anti-friction)
                                                                    Parameters                   Limits
               Parameter                Limits
                                                                     . 1  l i O  s i v  c o  y t i s  f f o  s p e c  5 0 %
               1. Bearing housing vibration (peak)                  2. Lube oil water content    below 200 ppm
                   a r  l a i d           4 . 0  s / n i  e c  1 (  0  m m  s /  e  ) c  3. Auxiliary oil pump operating yes/no  operating
                  a  l a i x              3 . 0  s / n i  e c  1 (  m m  s /  e  ) c  4. Bypass valve position (P.D.pumps)  change > 20%
               2. Bearing housing temperature  185 ° F(85°C)        5. Temperature control valve position  Closed, supply
               3. Lube oil viscosity    off spec 50%                                             temperature > 130 55°C)
               4. Lube oil particle size                            6. Filter P                  > 25 psid (170 kpag)
                  non metallic          > 25 microns                7. Lube oil supply valve position  change >  20%
                  m    c i l l a t e    a n y m a g n  c i t e  p  e l c i t r a  s  h t i w  s u m p
               5. Lube oil water content  below 200 ppm
                                                                   Fig 10.11.12   Condition monitoring parameters and their alarm limits

              Fig 10.11.9   Condition monitoring parameters and their alarm limits

                                                                    Pump sealflush (single seal, flush from discharge)

                                                                    Parameter        Limits
               Thrust bearing (hydrodynamic)
                                                                    1. Flush line     / 20°F ( / 10°C) of pump case
               Parameter                    Limits                    temperature    temperature
                                                                    2. Seal chamber  < 25 psi (175 kpa) above suction pressure
               1. Axial displacement*       > 15–20 mils (0.4–0.5 mm)  pressure
               2. Thrust pad temperature    220 ° F (105°C)
               3. Lube oil supply temperature  140  ° F (60°C)
               4. Lube oil drain temperature  190 ° F (90°C)       Fig 10.11.13   Condition monitoring parameters and their alarm limits
               5. Lube oil viscosity        off spec 50%
               6. Lube oil particle size    > 25 microns
               7. Lube oil water content    below 200 ppm
               *and thrust pad temperatures > 220°F (105°C)
                                                                    1. Calibrated: pressure and temperature gauges and flow meter
                                                                    2. Know gas analysis and calculate k, z, m.w
              Fig 10.11.10   Condition monitoring parameters and their alarm limits  3. Perform as close to rated speed and flow as possible
                                                                    4. Relationships:
                                                                                                         k  1
                                                                                 LN
                                                                           N  1
                                                                         A.    =          B: EFFICIENCY poly =  k
                                                                            N                            n  1
                                                                                 LN
               Pump liquid mechanical seal                                                                n
               Parameter                 Limits
                                                                                       847.4      n
               1. Stuffing box pressure  < 25 psig (175 kpa)                     kgM   =  MW  T1  n  1  Z avg  p1  1
               2. Stuffing box temperature  Below boiling temperature for
                                       process liquid
                                                 °
                                             °
               3. Flush line temperature  +  /  20 F (10 C) from pump case
                                       temp                                           T1
                                                                                                      p1
               4. Primary seal vent pressure  > 10 psi (70 kpag)
                 (before orifice)
                On tandem seal arrangements only                    5. Compare to previous value, if decreasing trend exists greater
                Typical limit – there are exceptions (Sundyne Pumps)  than 10%,inspect at first opportunity
              Fig 10.11.11   Condition monitoring parameters and their alarm limits  Fig 10.11.14   Compressor performance condition monitoring

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