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Improvement of the thermochemical water splitting IS process by an electrochemical cell using a cation exchange membrane

机译:通过使用阳离子交换膜的电化学电池改善热化学水分解是通过电化学电池的方法

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One of the key reactions for efficient hydrogen production through the water splitting IS(Iodine-Sulfur) process is the Bunsen reaction (SO2+I2+2H2O= H2SO4+2HI). The Bunsenreaction was examined by an electrochemical cell featuring a cation exchange membrane asthe separator, using sulfuric acid dissolving sulfur dioxide as the anolyte and hydriodic aciddissolving iodine as the catholyte. In galvanostatic electrolysis, molality of H2SO4 in theanolyte and that of HI in the catholyte were increased up to 17.8 mol kg-H2O -1 and 14.9 molkg-H2O -1 at I2/HI = 1, respectively. These concentrations were far higher than the reportedones that were obtained by the Bunsen reaction carried out in the presence of large amount ofiodine (e.g. I2/HI=4). The optimal concentrations of anolyte and catholyte were discussedby changing only one parameter. I2/HI ratio had little effects on the required total voltagesuggesting that lower I2 concentration is desired for the efficient operation. H2SO4concentration was found to be lower than 16 mol kg-H2O -1 for anolyte. One of the importantparameter that should be corrected was water content of the cation exchange membraneduring the experimental especially for the higher concentrations of anolyte and catholyte.
机译:通过水分解的有效氢气产生的关键反应之一是(碘 - 硫)工艺是Bunsen反应(SO2 + I2 + 2H2O = H 2 SO 4 + 2HI)。通过具有阳离子交换膜哮喘分离器的电化学电池检查Bunsecreaction,使用二氧化硫作为阳极电解液和硫代酸的碘作为阴极电解液。在镀锌电解中,在Theanolyte中H2SO4的摩尔醇和在阴极电解液中的Hi,在I2 / Hi = 1分别增加至17.8molkg-H 2 O -1和14.9 Molkg-H 2 O -1。这些浓度远高于通过在大量的大量(例如I2 / HI = 4)存在下进行的Bunsen反应获得的寄生时间。讨论了阳极电解液和阴极电解液的最佳浓度仅改变一个参数。 I2 / Hi比对所需的总电压效果几乎没有影响,以便有效操作所需的较低I2浓度。发现H2SO4络合为阳极电解液低于16mol kg-H2O -1。应该纠正的重要公绩将是阳离子交换膜的含水量,特别是对于较高浓度的阳极电解液和阴极电解液。

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