Page 290 - Hydrocarbon Exploration and Production Second Edition
P. 290

Surface Facilities                                                    277


                                                       gas


                              free
                              gas

                                                                         oil
                                                                    dispersion
                        wet crude                                   band




                                                                         water

                           gas         water        oil       wet crude
             Figure 11.11  Continuous dehydration tank.

                For dehydration of very high viscosity crudes, heaters can be used in combination
             with dehydration tanks. The temperature to which the crude is heated is a function
             of the viscosity required for effective separation.
                If oil and water are mixed as an emulsion, dehydration becomes much more
             difficult. Emulsions can form as oil-in-water or water-in-oil if mixed production
             streams are subjected to severe turbulence, as might occur in front of perforations in
             the borehole or in a pump. Emulsions can be encouraged to break (or destabilise)
             using chemicals, heat or just gentle agitation. Chemical destabilisation is the most
             common method and laboratory tests would normally be conducted to determine
             the most suitable combination of chemicals.


             11.1.2.6. De-oiling
             Skimming tanks have already been described as the simplest form of de-oiling
             facility; such tanks can reduce oil concentrations down to less than 200 ppm but are
             not suitable for offshore operations. Plate coalescer vessels or hydrocyclones (shown
             in Figure 11.13) are generally used offshore and maybe used in tandem with other
             water-cleaning devices such as gas flotation units. The choice of de-oiling unit is
             influenced by throughput, variability of the feed (in terms of oil content), space and
             weight considerations.
                Another type of gravity separator used for small amounts of oily water, the oil
             interceptor, is widely used both offshore and onshore. These devices work by
             encouraging oil particles to coalesce on the surface of plates. Once bigger oil droplets
             are formed they tend to float to the surface of the water faster and can
             be skimmed off. A corrugated plate interceptor (CPI)isshown in Figure 11.12 and
             demonstrates the principle involved. Plate interceptors can typically reduce oil-in-water
             content to 50–150ppm.
                To reduce oil content to levels which meet disposal standards it is often necessary
             to employ rather more sophisticated methods. Two such techniques which can
             reduce oil in water to less than 40 ppm are gas flotation and hydrocyclone processes.
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