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Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH2PO4 Solution Electrodialysis

机译:NaH2PO4溶液电渗析过程中通过阴离子交换膜的磷酸阴离子的部分通量

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摘要

Electrodialysis (ED) with ion-exchange membranes is a promising method for the extraction of phosphates from municipal and other wastewater in order to obtain cheap mineral fertilizers. Phosphorus is transported through an anion-exchange membrane (AEM) by anions of phosphoric acid. However, which phosphoric acid anions carry the phosphorus in the membrane and the boundary solution, that is, the mechanism of phosphorus transport, is not yet clear. Some authors report an unexpectedly low current efficiency of this process and high energy consumption. In this paper, we report the partial currents of H2PO4, HPO42−, and PO43− through Neosepta AMX and Fujifilm AEM Type X membranes, as well as the partial currents of H2PO4 and H+ ions through a depleted diffusion layer of a 0.02 M NaH2PO4 feed solution measured as functions of the applied potential difference across the membrane under study. It was shown that the fraction of the current transported by anions through AEMs depend on the total current density/potential difference. This was due to the fact that the pH of the internal solution in the membrane increases with the growing current due to the increasing concentration polarization (a lower electrolyte concentration at the membrane surface leads to higher pH shift in the membrane). The HPO42− ions contributed to the charge transfer even when a low current passed through the membrane; with an increasing current, the contribution of the HPO42− ions grew, and when the current was about 2.5 ilimLev (ilimLev was the theoretical limiting current density), the PO43− ions started to carry the charge through the membrane. However, in the feed solution, the pH was 4.6 and only H2PO4 ions were present. When H2PO4 ions entered the membrane, a part of them transformed into doubly and triply charged anions; the H+ ions were released in this transformation and returned to the depleted diffusion layer. Thus, the phosphorus total flux, jP (equal to the sum of the fluxes of all phosphorus-bearing species) was limited by the H2PO4 transport from the bulk of feed solution to the membrane surface. The value of jP was close to ilimLev/F (F is the Faraday constant). A slight excess of jP over ilimLev/F was observed, which is due to the electroconvection and exaltation effects. The visualization showed that electroconvection in the studied systems was essentially weaker than in systems with strong electrolytes, such as NaCl.
机译:带有离子交换膜的电渗析(ED)是一种有前途的方法,可以从市政废水和其他废水中提取磷酸盐,从而获得廉价的矿物肥料。磷被磷酸的阴离子运输通过阴离子交换膜(AEM)。然而,尚不清楚哪种磷酸阴离子在膜和边界溶液中携带磷,即磷的传输机理尚不清楚。一些作者报告说,该过程的电流效率出乎意料的低,并且能耗高。在本文中,我们通过Neosepta AMX和Fujifilm AEM Type X报告了H2PO4 -,HPO4 2-和PO4 3-的部分电流。穿过0.02 M NaH2PO4进料溶液的耗尽扩散层的H2PO4 -和H + 离子的分流和跨膜电位差的函数被研究的膜。结果表明,阴离子通过AEM传递的电流比例取决于总电流密度/电位差。这是由于以下事实:由于浓差极化的增加,膜中内部溶液的pH随着电流的增加而增加(膜表面较低的电解质浓度导致膜中的pH升高)。即使当低电流通过膜时,HPO4 2-离子也有助于电荷转移。随着电流的增加,HPO4 2-离子的贡献增加,当电流约为2.5 ilim Lev 时(ilim Lev 是理论极限电流密度),PO4 3-离子开始通过膜携带电荷。然而,在进料溶液中,pH为4.6并且仅存在H 2 PO 4 s-sups离子。当H2PO 4 -离子进入膜时,部分离子转变为双电荷和三电荷的阴离子。 H + 离子在此转化过程中释放,并返回到耗尽的扩散层。因此,磷的总通量j P (等于所有含磷物质的通量之和)受H 2 PO 4 < / sub> -从大量的进料溶液传输到膜表面。 j P 的值接近i lim Lev / F(F是法拉第常数)。观察到j P 略高于i lim Lev / F,这是由于电对流和升华效应引起的。可视化显示,所研究系统中的电对流本质上比具有强电解质(如NaCl)的系统弱。

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