Page 474 - 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 .34
              the seal oil system would maintain a differential of 34.5 kPa (5  The supply system
              PSI) across the gas side seal, and the supply pressure to the gas
              side bushing and atmospheric bushing would be 172 kPA (25  Referring to definition of a seal oil system, it can be seen that its
              PSI). In this case, the differential across the gas side bushing  function is identical to that of a lube oil system, with one
              would remain constant at 34.5 kPA (5 PSI), but the atmospheric  exception. The exception is that the seal fluid must be delivered
              bushing differential pressure would increase from 34.5 to 172  to the seals at the specified differential pressure. Let’s examine
              kPA (5 to 25 PSI). As a result, a primary concern in any seal  this requirement further.
              liquid system is the assurance that the atmospheric bushing  Refer again to Figure 7.34.2. Notice that the atmospheric
              receives proper fluid flow under all conditions. After the seal  bushing downstream pressure is constant (atmospheric pres-
              fluid exits the seal chamber, it essentially returns through two  sure). However, the gas side bushing pressure is referenced to
              additional subsystems.                               the compressor process pressure. This pressure can and will
                                                                   vary during operation. If it were always constant, the re-
              C The atmospheric draining system                    quirement for differential pressure control would not be
                                                                   present in a seal system and would be identical to that of a
              The flow from the atmospheric bushing, if it does not  lubricating system. Another way of visualizing the systems is to
              directly enter the bearing system, will return to the seal oil  understand that the lube system utilizes differential pressure
              reservoir. In addition, flow from any downstream control valve  control as well, but the reference pressure (atmospheric pres-
              will also return through the atmospheric drain system to the seal  sure) is constant and consequently all control valves need only
              oil reservoir. Both these streams should be gas free since they  control lube oil pressure. However seal systems require some
              should not come in contact with the process gas.     means of constant differential pressure control (reference gas
                                                                   pressure to seal oil supply pressure). This objective can be
                                                                   accomplished in many different ways. Referring back to
              D The seal leakage system                            Figure 7.84 it can be seen that the supply system function is
                                                                   identical to that of a lube oil system with the exception that
              The fluid that enters the gas side bushing is controlled to  the liquid is referenced to a pressure that can vary and must be
              a minimum amount such that it can be either discarded or  controlled to maintain a constant differential between the
              properly returned to the reservoir after it is degassed. Typically,  referenced pressure and the seal system supply pressure.
              this amount is limited to less than 77 liters (20 gallons) per day  The sizing of the seal oil system components is also identical to
              per seal. Since this liquid is in contact with the high speed shaft  that of the lube oil system components. Refer back and observe
              it is atomized and combines with sealing gas to enter the leakage  the heat load and flow required of each seal is determined in
              system. This system consists of:                     a similar way to that of the bearings. Seals are tested at various
                                                                   speeds and a necessary flow is determined to remove the heat
              - An automatic drainer                               of friction under various conditions. The seal oil flow re-
              - A vent system                                      quirements and corresponding heat loads, are then tabulated
              - Degassing tank (if furnished)
                                                                   and pumps exchangers, filters, and control valves are sized
                The function of each component is as follows:      accordingly.
                                                                     The seal oil reservoir is sized in exactly the same way as
                The drainer
                The drainer contains the oil-gas mixture from the gas side  lube oil reservoir in our previous example. The only major
              seal. The liquid level under pressure in the drainer is controlled  difference between the component sizing of a seal and a
              by an internal float or external level control valve to drain oil  bearing is that the seal flows across the atmospheric bushing
              back to the reservoir or the de-gassing tank, as required.  will change with differential pressures. Every liquid compressor
                                                                   seal incorporates a double seal arrangement. The gas side
                The vent system
                The function of the seal oil drainer vent system is to  seal differential is held constant by system design. The atmo-
              ensure that all gas side seal oil leakage is directed to the  spheric side seal differential varies with varying seal reference
              drainer. This is accomplished by referencing the drainer vent  (process) pressure. Therefore, the total flow to the seals will
              to a lower pressure than the pressure present at the gas side  vary with process pressure and must be specified for maximum
              seal in the compressor. The drainer vent can be routed back  and minimum values when sizing seal system components.
              to the compressor suction, suction vessel or a lower pressure  Remembering the concept of an equivalent orifice, a compressor
              source.                                              at atmospheric conditions will require significantly less seal oil
                                                                   flow than it will at high pressure 1,380 kPa (200 PSI) condi-
                The degassing tank
                This vessel is usually a heated tank, with ample residence  tions. This is true since the differential across the atmospheric
              time (72 hours or greater) to sufficiently de-gas all seal oil such  seal and liquid flow will increase from a low value to a signifi-
              that it will be returned to the reservoir and meet the seal oil  cantly higher value, while the gas side bushing differential and
              specification (viscosity, flashpoint, dissolved gasses, etc.). These  liquid flow will remain constant provided seal clearances remain
              items will be discussed in detail later.             constant.
                We will now proceed to discuss each of the major sub-  Many seal system problems have been related to insufficient
              systems in detail, defining the function of each such that the  seal oil flow through the atmospheric bushing at low suction
              total operation of a seal system can be simplified.   pressure conditions. Close attention to the atmospheric drain



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