Page 416 - 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
                When supply flow equals exit flow, the pressure in any  We can see by referring back to ‘the concept of an equivalent
              equivalent vessel remains constant. If supply flow is less than  orifice’ that this equation is similar to that of an orifice. Natu-
              exit flow, the pressure reduces rapidly. The function of an ac-  rally, the only difference is that a valve is a variable orifice.
              cumulator can be easily understood by using this equivalent  Valves are sized using this concept of C v (valve coefficient).
              vessel concept. If a vessel is installed downstream of the  Each valve has a maximum C v . Depending on the type of in-
              equivalent vessel in Figure 7.13.3, during the period of reduced  ternal valve design, seats, plugs, and body, a valve will exhibit
              inlet flow the vessel would supply flow to the system. This is  a certain characteristic. Refer to Figure 7.13.4 which is a graph
              exactly the function of an accumulator.              of valve characteristics.
                Another example of using the equivalent vessel concept is as  Plotted on the ordinate (y axis) is valve flow in
              follows: Imagine again the equivalent vessel is a supply pipe from  percent of maximum flow and plotted on the abscissa (x axis) is
              a lube oil console. Suppose the main pump trips on overload,  travel of the valve plug in percent of rated travel. The char-
              and the auxiliary pump does not start immediately. Since the  acteristics of particular valves will be discussed when we cover
              auxiliary pump did not immediately start, the supply flow to  specific valve application later in this section. Referring back to
              the equivalent vessel is less than the exit flow. As a result, the  the relationship for a valve coefficient shows it to be dependent
              pressure in the equivalent vessel will drop. This is why pressure  on flow rate, differential pressure across the valve, and fluid
              switches in auxiliary systems are used as alarm, auxiliary pump  characteristics.
              start or trip devices. Using our concept of an equivalent vessel, it  As an example, suppose that a valve is sized to pass 20 GPM
              can be seen that the pressure switch actually acts as a flow in-  under normal conditions of 150 psi pressure drop. The fluid in
              dicator and will activate on low flow even though it is measuring  this case is light turbine oil at 150 F (60 SSU). Solving for the

              pressure.                                            valve C v with the above equation, we arrive at a figure of 1.51. If
                                                                   the valve pressure drop were to decrease to 100 lbs, and we still
                                                                   required 20 gallons per minute to pass, the valve coefficient
              Control valve liquid sizing coefficient e C v
                                                                   would be 1.84. This change represents approximately a 22%
              ‘C v ’ is an important concept that must be understood when  change in the valve coefficient. Depending on the characteristic
              dealing with any type of control valve in liquid service. C v , the  curve of the valve in question, it would represent a given amount
              ‘valve sizing coefficient’,is defined by the following equation:  of valve plug opening (increase of travel). In the same example,
                                           r ffiffiffiffiffiffiffiffiffiffi            now let us assume that the flow changes to 40 GPM with 100 lbs
                                             S:G:
                              C v ¼ Q ðGPMÞ                        pressure drop across the valve. The C v now would be 3.69 or
                                              DP
                                                                   approximately 200% of the previous value. Depending on the
              Where: S.G. (specific gravity) ¼ 0.85 (for oil)       valve size, this coefficient may or may not be obtainable. Refer
                6P ¼ value pressure drop (psi)                     to Figure 7.13.5 which is a typical valve coefficient table
                                                                   showing valve coefficients for % travel of a particular valve.
                Solving this equation for GPM we see that:
                                                                   When sizing all control valves, C v maximum, C v normal and C v
                                            C v                    minimum must be calculated. A general rule is that all of the
                               QðGPMÞ¼ r    ffiffiffiffiffiffiffiffiffiffi
                                            S:G:                   above values should fall between 10% and 90% of the maximum
                                            DP                     C v for a particular valve selected.


                                                                              Fig 7.13.4   Control valve flow characteristics
                                                                              (Courtesy of Fisher Controls Inc.)





























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