Page 222 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 3 .22          Compressor Best Practices


















































       Fig 3.22.10   API 614 Lube-seal oil system for ISO-carbon seals (Courtesy of Elliott Company)


          As an example, if the required gas side seal differential of oil  In the above example, at 1,380 kPa (200 psi) reference
       to gas is 34.5 kPad (5 psid), by the liquid head equation:  pressure, the bypass valve would close considerably. To increase
                                                            the pressure supply of the seal oil from 34.5 to 1,413 kPa (5 to
                        0:102   34:5
                 Head ¼             ¼ 4:1 meters            205 psi), the difference of bypass flow through the valve, of
                            0:85                            37 lpm (7 gpm), is equal to the increased flow through the
                         2:311   5 psid
                 ðHead ¼             ¼ 13:6ft:Þ
                             0:85
                                                             Table 3.22.1 Seal System Flow
          Therefore maintaining a liquid level of 4.1 meters (13.6 ft)
       above the seal while referencing process gas pressure will ensure  Item  Start-up condition  Normal operation
       a continuous 34.5 kPad (5 psid) gas side bushing differential. In
       this configuration, the control valve, which senses its signal from  Compressor suction  0 kPa (PSIG)  1,380 kPa (200 PSIG)
                                                             pressure
       the level transmitter, will be sized to continuously supply the
       required flow to maintain a constant level in the overhead tack.  Overhead tank reference  0 kPa (PSIG)  1,380 kPa (200 PSIG)
       As an example, consider the following system changes from  pressure
       start-up to normal operation.                         Gas side seal bushing flow  0 LPM (GPM)  0 LPM (GPM)
          In this example, a change from the start-up to operating
       condition will increase gas reference pressure on the liquid level  Atmospheric side seal  19.3 LPM (5 GPM)  46 LPM (12 GPM)
       in the overhead tank, and would tend to push the level down-  bushing flow
       ward. Any movement of the level in the tank will result in an  Seal pump flow  77 LPM (20 GPM)  77 LPM (20 GPM)
       increasing signal to the level control valve to open, thus in-
       creasing the pressure (assuming a positive displacement pump)  Bypass valve flow  57.8 LPM (15 GPM)  30.8 LPM (8 GPM)
       to the overhead tank and reestablishing the pre-set level.

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