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Backpulsing fouling control with membrane recovery of light non-aqueous phase liquids.

机译:通过膜回收轻质非水相液体进行反脉冲结垢控制。

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摘要

Membrane recovery of light non-aqueous phase liquids (LNAPLs) was studied. Small membrane modules, operated in a sealed end configuration, were pressurized with several LNAPLs in order that membrane permeability and fouling processes might be characterized. The mitigation of membrane fouling via backpulsing was optimized for backpulse amplitude, frequency, and duration. A full-scale LNAPL recovery device was tested in the laboratory. Clean-membrane permeability was determined via single-fiber extraction of 2-propanol, distilled kerosene, commercial kerosene, commercial diesel fuel, and LNAPL obtained from the subsurface of a contaminated refinery site. Membrane fouling occurred during laboratory extraction of commercial kerosene, distilled kerosene, and the refinery fluid, but not for 2-propanol. Filtration experiments showed suspended solids present within the LNAPLs. Scanning electron microscope images of fouled membranes indicated that these solids were deposited upon the membrane surface. The fouling was due to pore blockage, pore constriction, and/or cake layer formation. The use of backpulsing was found to mitigate pore constriction and cake layer formation. Backpulsing improved recovery rates by ∼ 30% over a 15 hr period, but it could not prevent the occurrence of some irreversible fouling. The device designed to fit into a typical recovery well extracted ∼ 35% of the volume expected for given operating pressures and clean membrane permeability, under non-fouling conditions. The less than optimal performance was due to crimping of hollow fibers during the potting process, and not fiber-fiber interactions. Under non-fouling conditions, field operation of the device can yield 1-2000 L/day, which is a theoretical range of subsurface LNAPL recharge rates. With the use of backpulsing under fouling conditions, the membrane recovery device can extract up to 50 L/day, but this must be coupled with regular cleaning/replacement of the membranes.
机译:研究了轻质非水相液体(LNAPL)的膜回收率。在几个密封的末端结构中运行的小型膜组件,用几个LNAPL加压,以表征膜的渗透性和结垢过程。针对反脉冲幅度,频率和持续时间优化了通过反脉冲减轻膜污染的方法。全面的LNAPL回收设备在实验室中进行了测试。通过2-丙醇,蒸馏煤油,商业煤油,商业柴油和从受污染的炼油厂地下获得的LNAPL的单纤维萃取来确定清洁膜的渗透性。在实验室萃取商业煤油,蒸馏煤油和炼油厂的流体时发生了膜结垢,但对于2-丙醇则没有。过滤实验显示LNAPL中存在悬浮固体。结垢膜的扫描电子显微镜图像表明,这些固体沉积在膜表面上。结垢是由于孔堵塞,孔收缩和/或滤饼层的形成。发现使用反脉冲可以减轻孔收缩和滤饼层的形成。反脉冲在15小时内将回收率提高了约30%,但不能防止发生某些不可逆的结垢。该设备设计为适合典型的回收井,在不结垢的条件下,提取了给定操作压力和干净的膜渗透性预期的〜35%的体积。达不到最佳性能的原因是在灌封过程中中空纤维的卷曲,而不是纤维与纤维之间的相互作用。在无污垢条件下,该设备的现场操作可产生1-2000 L / day,这是地下LNAPL补给速率的理论范围。通过在结垢条件下使用反冲,膜回收装置每天可提取多达50 L的水,但必须与定期清洁/更换膜相结合。

著录项

  • 作者

    McAlexander, Benjamin L.;

  • 作者单位

    University of Wyoming.;

  • 授予单位 University of Wyoming.;
  • 学科 Engineering Environmental.
  • 学位 M.S.
  • 年度 2003
  • 页码 62 p.
  • 总页数 62
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 环境污染及其防治;
  • 关键词

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