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A study of concentration polarization and solution-membrane interactions in the electrodialytic desalination process.

机译:电渗析脱盐过程中浓度极化和溶液-膜相互作用的研究。

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摘要

The problem of concentration polarization in electrodialytic desalination occurs due to mass transfer limitations within thin film layers adjacent to anion and cation exchange membranes. Each type of membrane behaves quite differently in electrodialysis. Anion exchange membranes promote water ionization while cation exchange membranes do not. Control of water ionization is desirable since it limits process efficiency. Studies have been conducted to better understand the nature of each solution-membrane interface and suggest why each behaves differently.;Experiments designed to promote concentration polarization (interfacial ionic depletion) have been conducted for characterization of several different ion exchange membranes by their limiting current behavior as a function of flow velocity in a small 9 x 10 membrane stack. The Nernst film model was employed along with an analogy between heat and mass transfer for a flat plate for comparison of experiment and theory. Results for anion exchange membranes were in good agreement with theory whereas cation exchange membranes exhibited limiting currents well beyond those theoretically expected.;Theoretical quantum mechanical calculations indicate that stronger ion-solvent interactions exist for ions present at cation exchange membrane-solution interfaces (;Spectroscopic experiments in the 1300-1800 nm region of the near infrared suggest that interactions having a significantly greater effect on water structure are present in the case of concentrated (2N) solutions containing a cation exchange membrane solution analogue (p-toluenesulfonic acid, sodium salt) relative to similar solutions containing an anion exchange analogue (benzyl-trimethylammonium chloride).;In the final analysis, modifications to solvent (water) structure are believed due to the nature of ion hydration in the vicinity of the cation exchange membrane-solution interface. Along with the presence of high electric fields induced by polarization in the interface region that increase exchange rates of primary hydration water with bulk water due to accelerated dipole reorientation (75), the combined effects may enhance cation mobility/diffusivity under these conditions. The result then being a suppression of water ionization at cation exchange membranes due to the enhanced flux, versus absence of a similar effect at anion exchange membranes.
机译:由于与阴离子交换膜和阳离子交换膜相邻的薄膜层内的传质限制,发生了电渗析脱盐中的浓差极化问题。每种类型的膜在电渗析中的行为都大不相同。阴离子交换膜可促进水离子化,而阳离子交换膜则不会。水电离的控制是合乎需要的,因为它限制了工艺效率。已经进行了研究以更好地理解每种溶液-膜界面的性质,并指出每种溶液为何表现不同。;已经进行了旨在促进浓度极化(界面离子耗竭)的实验,以通过限制电流行为表征几种不同的离子交换膜在9 x 10的小型膜堆中作为流速的函数。 Nernst薄膜模型与平板传热和传质之间的相似性用于实验和理论的比较。阴离子交换膜的结果与理论吻合良好,而阳离子交换膜的极限电流远远超出了理论上的预期。;理论量子力学计算表明,存在于阳离子交换膜-溶液界面的离子存在更强的离子-溶剂相互作用(;在近红外1300-1800 nm区域进行的实验表明,在含有阳离子交换膜溶液类似物(对甲苯磺酸,钠盐)的浓缩(2N)溶液的情况下,对水结构的相互作用具有明显更大的影响相对于含有阴离子交换类似物(苄基三甲基氯化铵)的类似溶液。在最终分析中,由于阳离子交换膜-溶液界面附近离子水合的性质,据信对溶剂(水)结构进行了修饰。随着极化产生的高电场的存在由于加速偶极子重新定向,界面区域中的水合反应增加了初级水合水与大量水的交换率(75),在这些条件下,综合作用可增强阳离子迁移率/扩散性。然后结果是由于通量的增加而抑制了阳离子交换膜上水的电离,而阴离子交换膜上却没有类似的作用。

著录项

  • 作者

    Irwin, Kenneth James.;

  • 作者单位

    University of Rhode Island.;

  • 授予单位 University of Rhode Island.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 1988
  • 页码 419 p.
  • 总页数 419
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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