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STUDIES ON SULFUR-IODINE THERMOCHEMICAL CYCLE FOR HYDROGEN PRODUCTION

机译:用于制氢的硫碘热化学循环研究

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We report here the work that has been initiated at the Chemistry Division, on Sulfur-Iodine thermochemical cycle, which deals with the development of catalyst systems for decomposition of suifuric acid, the most energy intensive step involved in this cycle towards decomposition of water for hydrogen production. Chromium substituted Fe_2O_3, catalysts were synthesized via solid-state route and characterized by XRD, N_2sorption and Temperature Programmed Reduction/Oxidation (TPR/O) techniques. Catalytic activity for decomposition of suifuric acid in temperature range of 400 - 800 deg C has shown, that onset temperature for SO_2 formation in all samples was ~600°C. Successive TPR/O studies on these samples have revealed better sintering characteristics as compared to a pure Fe_2O_3 sample and thereby suggested a better performance of chromium substituted catalyst, during prolonged use for suifuric acid decomposition.
机译:我们在这里报告化学司关于硫-碘热化学循环的工作,该工作涉及开发用于分解硫酸的催化剂体系,该体系是该循环朝水分解为氢的过程中最耗能的步骤生产。通过固相合成铬取代的Fe_2O_3催化剂,并通过XRD,N_2吸附和程序升温还原/氧化(TPR / O)技术对其进行表征。已显示在400-800℃的温度范围内分解为亚硫酸的催化活性,所有样品中SO_2形成的起始温度均为〜600°C。对这些样品进行的连续TPR / O研究表明,与纯Fe_2O_3样品相比,烧结性能更好,从而表明在长期使用硫酸盐分解过程中,铬取代的催化剂具有更好的性能。

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