Page 52 - Oil and Gas Production Handbook An Introduction to Oil and Gas Production
P. 52

•   Larger oil  and gas
               installations  use
               centrifugal
               compressors with 3-
               10 radial wheels,
               6000–20000     rpm
               (highest for small
               size), up to  80 MW
               load at discharge
               pressure of up to 50
               bars   and    inlet
               volumes of up to
                           3
               500,000    m /hour.
               Pressure differential
               up      to     10.
               Photo: Dresser Rand
        Most compressors will not  cover the full pressure  range efficiently. The
        lowest pressure is atmospheric, for gas to pipeline, some 3 to 5 MPa (30-50
        bar) pressure is used, while reservoir reinjection of gas will typically require
        20 MPa (200 bar) and upwards since there is no liquid in the tubing and the
        full reservoir pressure must be overcome. Therefore compression is divided
        into several stages to improve maintenance and availability.
        Also due to  single unit power limitations, compression is often divided in
        several parallel trains. This is not the case in this example since gas is not
        exported, and reinjection can be interrupted during maintenance periods.
        Compressors are driven by gas turbines or electrical motors (for lower power
        also  reciprocating engines, steam turbines  are sometimes used if  thermal
        energy is available). Often several stages in the same train are driven by the
        same motor or turbine.
        The main operating parameters for a compressor are the flow and pressure
        differentials. The product defines the total loading, so there is a ceiling set by
        the maximum design  power.  Furthermore, there is a  maximum differential
        pressure (Max P d) and choke flow (Max Q), the maximum flow that can be
        achieved. At lower flow, there is  a minimum pressure differential and flow
        before the compressor will "surge" if there is not enough gas to operate. If
        variations in flow are expected  or  difference between common shaft
        compressors will occur, the situation  will be handled with  recirculation. A
        high flow, high pressure differential surge control valve will open to let gas
        from the discharge side back into the suction side. Since this gas is heated it
        will also pass through the heat exchanger  and scrubber  not  to become
        overheated by circulation.


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