Is paper WS selected for presentation by an SPE Program committee following review of information cnntained in an abstract submitted by the author(s). Contents of the paper, as presented, have not been revtewed by the S@ety of Petroleum Englneera and are subject to mrretion by the author(s). The material, as presented, does not neceaearlly reflect anỹ ition of the society of Petroleum Engineers, ita ofricera, w members. Papers presented at SPE meetings are subject to pubK@tion retiew by Editorial Committees of the Scdety of Petroleum Englneara. Electronic reproduction, distribution, or storage of any part of this paper for mmmerdal pu~ee tithwt the written mnsent of the Sdety of Petroleum Engineers Is prohibited. Permission to raproduce In print is restricted to an absbad of not more than 300 wurds; illustrations may not be mpied.The abstrad must mntsln wnsplcuous atiowledgment of Mere and by whom the paper was preeented. Write Librartan, SPE, P.O. Mx 833636, Ritiardson, TX 7S0S3-3836, U.SA., fax 01 -972-952-%3S. AbstractFor oil production under high water cut conditions the efforts needed for de-oiling of the production water are mainly determined by the oil-droplet-size distribution of this water. This distribution is predominantly the result of droplet breakup in the choke valve. To determine the effect of the choke valve on the droplet-size distribution, we have conducted laboratory experiments in which we used a circular orifice in a circular pipe. With the help of theory on droplet break-up in turbulent flow and with knowledge of the flow field inside an orifice, a prediction of the distribution after break-up can be made. It is shown that the droplets increase in size with increasing oil viscosity and Mermore it appears that, for the description of the break-up process, the distribution of the turbulence over the orifice zone is an important factor.
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