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Modeling electrostatic separation for dehydration and desalination of crude oil in an industrial two-stage desalting plant

机译:工业两级脱盐工厂中用于原油脱水和脱盐的静电分离建模

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The aim of present study is to develop a mathematical model to predict water and salt separation efficiencies in an industrial two stages crude oil desalting process. The considered process consists of mixing valve and electrostatic drums connected in series. The desalting plant is modeled based on the population balance method considering water droplet breakage and coalescence terms to predict droplet size distribution. The class method as a common mathematical technique is selected to solve population balance equation. The accuracy of the developed mathematical model and considered assumption is evaluated using taken data from an industrial desalting plant. Then, the effect of mixing valve pressure drop, flow rate of fresh water and strength of electric field is studied on the desalting and dehydration efficiencies. The simulation result shows that increasing flow rate of fresh water from 3% to 6% decreases salt content in the treated crude oil from 2.06 to 0.71 PTB. (C) 2015 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:本研究的目的是建立一个数学模型来预测工业两步原油脱盐过程中水和盐的分离效率。考虑的过程包括串联连接的混合阀和静电鼓。基于人口平衡方法对脱盐工厂进行建模,该方法考虑了水滴的破裂和聚结项以预测水滴的大小分布。选择作为通用数学技术的分类方法来求解人口平衡方程。使用来自工业脱盐厂的数据评估开发的数学模型和考虑的假设的准确性。然后,研究了混合阀的压降,淡水的流量和电场强度对脱盐和脱水效率的影响。模拟结果表明,将淡水的流量从3%增加到6%,可将处理后的原油中的盐含量从2.06 PTB降低到0.71 PTB。 (C)2015台湾化学工程师学会。由Elsevier B.V.发布。保留所有权利。

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