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In-Line Testing of Novel Filter Media for Oil-Water Mixtures

机译:油水混合物新型过滤介质的在线测试

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摘要

Proof-of-concept of novel, nano-fibrous, highly selective and inexpensive filter media for in-line oil-water separation is established. Two kinds of filter membranes were fabricated, hydrophobic-oleophilic membrane and hydrophilic-oleophobic membrane. Three housing configurations were designed, namely dead-end, crossflow (inside-out) and "outside-in" crossflow, incorporating the filter membranes, and tested in a multiphase flow loop. The recommended design, the "outside-in" crossflow configuration, consisted of a 2" diameter outer pipe and an inner porous tube of 3/4" diameter, around which the filter membrane was wrappedl.;Experimental runs were conducted with only the hydrophilic-oleophobic filter for water-continuous flow with low oil concentrations (water cleaning). The collected experimental data included pressure drop, permeate flow rate and purity. Values of permeate flow rate and pressure drop were averaged over the duration of the experiments, which was about 5 minutes, constituting the "initial average" of the permeate flow rate and the corresponding pressure drop.;The "outside-in" crossflow filter housing configuration showed the best performance as it provided robustness and durability for the filter membrane. Twelve experimental runs were conducted with the "outside-in" housing configuration for mixture velocities of 0.038 m/s, 0.055 m/s and 0.066 m/s, and oil concentrations of 0.6%, 0.83%. 1.1%, 7.9% and 9.1%.;Permeate samples were analyzed for oil content and showed high average separation efficiency of 98 + 2%. The permeate flux across the filter cartridge ranged between 0.0739 (L/h)/cm2 to 0.216 (L/h)/cm2 owing to the low pressure drop. Oil concentration in permeate water samples showed consistently increasing trend with an increase in inlet oil content, while maintaining high separation efficiency for all runs. The pressure drop across the membrane under flowing conditions ranged from 0.35 psid to 0.6 psid for flow rates between 0.1 L/min and 0.29 L/min, respectively. The filter membrane breakthrough pressure was 0.35 psid.
机译:建立了用于在线油水分离的新型,纳米纤维,高选择性和廉价过滤介质的概念验证。制备了两种滤膜,疏水-亲油膜和亲水-疏油膜。设计了三种外壳配置,即无端,​​错流(由内向外)和“由外而内”的错流,并结合了滤膜,并在多相流回路中进行了测试。推荐的设计是“由外而内”的错流配置,它由一个直径为2英寸的外管和一个直径为3/4英寸的内部多孔管组成,滤膜缠绕在该多孔管周围。;仅在亲水性条件下进行实验-疏油过滤器,用于低油浓度的水连续流动(水清洁)。收集的实验数据包括压降,渗透液流速和纯度。在整个实验过程中(大约5分钟)对渗透物流速和压降值取平均值,构成了渗透物流速和相应压降的“初始平均值”。构型显示出最佳性能,因为它为滤膜提供了坚固性和耐用性。使用“外向内”外壳配置进行了十二次实验,混合物速度分别为0.038 m / s,0.055 m / s和0.066 m / s,油浓度为0.6%,0.83%。 1.1%,7.9%和9.1%.;分析了渗透样品中的油含量,显示出98 + 2%的高平均分离效率。由于低压降,穿过滤筒的渗透通量在0.0739(L / h)/ cm2至0.216(L / h)/ cm2之间。渗透水样品中的油浓度显示出随着进口油含量的增加而持续增加的趋势,同时保持了所有运行的高分离效率。在流速为0.1 L / min和0.29 L / min之间的流动条件下,跨膜的压降范围为0.35 psid至0.6 psid。滤膜穿透压力为0.35 psid。

著录项

  • 作者

    Mule, Anisha.;

  • 作者单位

    The University of Tulsa.;

  • 授予单位 The University of Tulsa.;
  • 学科 Petroleum engineering.
  • 学位 M.Sc.
  • 年度 2017
  • 页码 92 p.
  • 总页数 92
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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