کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
155743 | 456910 | 2012 | 8 صفحه PDF | دانلود رایگان |

The breakup of crude oil emulsions to produce clean oil and water phases is an important task in crude oil processing. We have investigated the demulsification kinetics of a model oil-in-water emulsion in a centrifugal field to mimic the forces acting on emulsion droplets in oil/water separators such as hydrocyclones. The rate of growth of separated oil phase and the change in mean droplet diameter of the emulsion layer was measured as a function of surfactant concentration, centrifugal acceleration and time. Demulsification is enhanced with increasing centrifugal acceleration and time and decreasing surfactant concentration. A kinetic analysis was performed that allows to estimate the characteristic coalescence times between droplets in the emulsion and between a droplet and the separated oil interface. The experimental procedure presented in this work can serve as a simple, but useful test to predict the separation efficiency of emulsions in separators with swirling flow fields.
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► We present a simple method to assess the stability of emulsions in centrifugal flow fields.
► The change in drop size and growth of pure oil phase in an O/W emulsion was measured.
► A kinetic model is presented that allows calculation of characteristic coalescence times.
► The procedure may be of help for the petroleum industry in choosing a separator for a given produced fluid.
Journal: Chemical Engineering Science - Volume 71, 26 March 2012, Pages 118–125