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Guo, Boyun / Computer Assited Petroleum Production Engg 0750682701_chap11 Final Proof page 137  3.1.2007 8:54pm Compositor Name: SJoearun




                                                                              TRANSPORTATION SYSTEMS  11/137
                         Rotary compressors are divided into two classes: the  floor space for the quantity of gas removed, and it has
                       centrifugal compressor and the rotary blower. A centrifu-  almost pulsation-less flow. As its disadvantages, it cannot
                       gal compressor (Fig. 11.4) consists of a housing with flow  withstand high pressures, it has noisy operation because of
                       passages, a rotating shaft on which the impeller is  gear noise and clattering impellers, it improperly seals the
                       mounted, bearings, and seals to prevent gas from escaping  clearance between the impellers and the casing, and it
                       along the shaft. Centrifugal compressors have few moving  overheats if operated above safe pressures. Typically,
                       parts because only the impeller and shaft rotate. Thus, its  rotary blowers deliver a volumetric gas flow rate of up to
                       efficiency is high and lubrication oil consumption and  17,000 cfm and have a maximum intake pressure of
                       maintenance costs are low. Cooling water is normally  10 psig and a differential pressure of 10 psi.
                       unnecessary because of lower compression ratio and  When selecting a compressor, the pressure–volume
                       lower friction loss. Compression rates of centrifugal com-  characteristics and the type of driver must be considered.
                       pressors are lower because of the absence of positive dis-  Small rotary compressors (vane or impeller type) are gen-
                       placement. Centrifugal compressors compress gas using  erally driven by electric motors. Large-volume positive
                       centrifugal force. In this type of compressor, work is  compressors operate at lower speeds and are usually
                       done on the gas by an impeller. Gas is then discharged at  driven by steam or gas engines. They may be driven
                       a high velocity into a diffuser where the velocity is reduced  through reduction gearing by steam turbines or an electric
                       and its kinetic energy is converted to static pressure.  motor. Reciprocation compressors driven by steam tur-
                       Unlike reciprocating compressors, all this is done without  bines or electric motors are most widely used in the natural
                       confinement and physical squeezing. Centrifugal compres-  gas industry as the conventional high-speed compression
                       sors with relatively unrestricted passages and continuous  machine. Selection of compressors requires considerations
                       flow are inherently high-capacity, low-pressure ratio ma-  of volumetric gas deliverability, pressure, compression
                       chines that adapt easily to series arrangements within  ratio, and horsepower.
                       a station. In this way, each compressor is required to  The following are important characteristics of the two
                       develop only part ofthe station compression ratio. Typically,  types of compressors:
                       the volume is more than 100,000 cfm and discharge
                       pressure is up to 100 psig.               . Reciprocating piston compressors can adjust pressure
                         A rotary blower is built of a casing in which one or more  output to backpressure.
                       impellers rotate in opposite directions. Rotary blowers are  . Reciprocating compressors can vary their volumetric
                       primarily used in distribution systems where the pressure  flow-rate output (within certain limits).
                       differential between suction and discharge is less than  . Reciprocating compressors have a volumetric efficiency,
                       15 psi. They are also used for refrigeration and closed  which is related to the relative clearance volume of the
                       regeneration of adsorption plants. The rotary blower has  compressor design.
                       several advantages: large quantities of low-pressure gas  . Rotary compressors have a fixed pressure ratio, so they
                       can be handled at comparatively low horsepower, it has  have a constant pressure output.
                       small initial cost and low maintenance cost, it is simple to  . Rotary compressors can vary their volumetric flow-rate
                       install and easy to operate and attend, it requires minimum  output (within certain limits).
                                          Inlet
                                          diaphragm
                                                           Interstage
                                 Impeller                  diaphragm                  Outer spacer
                               Guide                                                  Exit guide vane
                               vane
                                                                                        Rotor spacer

                            Suction                                                          Discharge
                            bearing                                                          bearing
                            and seal                                                         and seal
                            housing                                                          housing











                             Stub shaft
                                                                                            Moving
                                                                                            parts

                                                                                            Stationary
                                                                                            parts

                            Figure 11.4 Cross-section of a centrifugal compressor (courtesy of Petroleum Extension Services).
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