Page 44 - Oil and Gas Production Handbook An Introduction to Oil and Gas Production
P. 44

separator to about 3-5  MPa (30-50 times  atmospheric pressure). Inlet
        temperature is often in the range of 100-150 degrees  C.  On the example
        platform, the well stream is colder due to subsea wells and risers.

        The pressure is  often
        reduced   in   several
        stages, in this instance
        three  stages are used
        to allow the controlled
        separation of volatile
        components. The idea
        is to achieve maximum
        liquid  recovery  and
        stabilized oil  and gas
        and to  separate water.
        A    large   pressure
        reduction in  a single  separator will cause flash vaporization leading to
        instability and safety hazards.

        The retention period is typically 5 minutes, allowing the gas to bubble out,
        water to settle at the bottom and oil to  be taken out in the middle. In this
        platform the  water cut (percentage  water in the  well flow) is almost 40%
        which is quite high. In the first stage separator, the water content is typically
        reduced to less than 5%.

        At the crude entrance, there is a  baffle  slug catcher that will  reduce the
        effect of slugs (large gas bubbles or liquid plugs). However some turbulence
        is desirable as this will release gas bubbles faster than a laminar flow.

        At the end, there are barriers  up to a certain level to keep  back the
        separated oil and water. The main control loops are the oil level control loop
        (EV0101 20 above) controlling the oil flow out of the separator on the right,
        and the gas pressure loop at the top.(FV0105 20 above) These loops are
        operated by the Control System. An important function is also to prevent gas
        blow-by which happens when a low oil level causes gas to exit via the oil
        output causing high pressure downstream. There are generally many more
        instruments and control  devices mounted on the separator. These  will be
        discussed later.

        The liquid outlets from the separator will be equipped with vortex breakers
        to reduce disturbance on the liquid table inside. This is basically a flange trap
        to break any vortex formation and ensure that only separated liquid is tapped
        off and not mixed with oil or water drawn in though these vortices. Similarly


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