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176    Environmental Control in Petroleum Engineering


   Hydrocyclones for separating oil and water are limited to cases where
 the inlet pressure is sufficient to drive the flow (Flanigan et al., 1989).
 For low-pressure operations, the fluid may need to be pumped into the
 hydrocyclone. A progressive cavity pump with low shear has been found
 to be an effective way to increase the fluid pressure without shearing the
 oil into smaller drop sizes. The drop size is a critical parameter in the
 effectiveness of hydrocyclones in separating oil from water.
   A related way to enhance gravity separation is through a decanting
 centrifuge. In this device, the produced water enters the spinning
 centrifuge, where the oil is separated from the water because of its
 lower density. Centrifuges differ from hydrocyclones in that the
 spinning is mechanically driven in a centrifuge, while it is induced
 by the inlet velocity of the water in a hydrocyclone. A centrifuge can
 also have internal plates to enhance separation, making it a spinning
 plate separator. Centrifuges can remove oil droplets down to about 2
 micrometers in diameter (Van Den Broek and Plat, 1991).

 Heater Treaters

   Oil and water can also be separated by heating the mixture. The
 higher temperature lowers the fluid viscosity of the mixture and alters
 the interfacial tension between the phases, allowing the oil and water
 to separate faster.

 Gas Flotation


   Suspended oil droplets can also be removed from water by gas
 flotation. If gas bubbles are passed through an emulsion of oil-in-water,
 the oil droplets will attach to the bubbles and be carried to the top of
 the mixture where they can be easily removed. Air bubbles are norm-
 ally pumped through the water, although the expansion of dissolved
 air is also used. Gas flotation is often aided by the addition of chemical
 coagulants. Carbon dioxide has also been used as the flotation gas
 (Burke et al., 1991). Gas flotation, however, can create a foam that is
 difficult to break.
   Gas flotation systems can reduce oil concentrations to 15-100 mg/1,
 with a typical average of 40 mg/1 (Simms et al., 1990). Like other
 separation methods, gas flotation systems can have operational difficul-
 ties, as summarized in Table 6-1.
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