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A WALL FILM MODEL FOR MEMBRANE FOULING

机译:膜污染的壁膜模型

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Deoiling of produced or impaired waters associated with oil and gas production represents a significant challenge for many companies. Centrifugation, air flotation, and hydrocyclone separation are the current methods of oil removal from produced water [1], however the efficiency of these methods decreases dramatically for droplets smaller than approximately 15-20 μm. More effective separation of oil-water mixtures into water and oil phases has the potential to both decrease the environmental footprint of the oil and gas industry and improve human well-being in regions such as the Gulf of Mexico. New membrane separation processes and design of systems with advanced flow management offer tremendous potential for improving oil-water separation efficacy. However, fouling is a major challenge in membrane separation [2]. In this study, the behavior of oil droplets and their interaction with crossflow filtration (CFF) membranes (including membrane fouling) is studied using computational fluid dynamics (CFD) simulations. A model for film formation on a membrane surface is proposed for the first time to simulate film formation on membrane surfaces. The bulk multiphase flow is modeled using an Eulerian-Eulerian multiphase flow model. A wall film is developed from mass and momentum balances [3] and implemented to model droplet deposition and membrane surface blockage. The model is used to predict film formation and subsequent membrane fouling, and allow to estimate the actual permeate flux. The results are validated using available experimental data.
机译:与石油和天然气生产相关的产出水或受损水的脱油对许多公司而言是一项重大挑战。离心,气浮和水力旋流器分离是目前从采出水中去除油的方法[1],但是对于小于约15-20μm的液滴,这些方法的效率会大大降低。更有效地将油水混合物分离为水相和油相,有可能减少石油和天然气行业的环境足迹,并改善墨西哥湾等地区的人类福祉。新的膜分离工艺和具有先进流量管理系统的设计为提高油水分离效率提供了巨大的潜力。然而,结垢是膜分离中的主要挑战[2]。在这项研究中,油滴的行为及其与错流过滤(CFF)膜(包括膜结垢)的相互作用使用计算流体动力学(CFD)模拟进行了研究。首次提出了在膜表面形成膜的模型,以模拟在膜表面形成膜的过程。使用Eulerian-Eulerian多相流模型对整体多相流进行建模。壁膜是由质量和动量平衡[3]开发而成的,可用来模拟液滴沉积和膜表面阻塞。该模型用于预测膜形成和随后的膜污染,并允许估计实际的渗透通量。使用可用的实验数据验证结果。

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