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Carbon monoxide separation by reactive absorption in chlorocuprate(I)-based ionic liquid

机译:通过反应性吸收在氯化物(I)的离子液中的反应吸收分离一氧化碳分离

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1.Introduction High amounts of CO are often release in the waste gas streams of industrial processes when a partial combustion of hydrocarbons is performed, e.g. carbon black manufacturing, steel-making and silicon carbide processes. The selective recovery and valorisation of this CO could be sought as a means to obtain a valuable by-product such as hydrogen or chemicals, e.g. methanol, formaldehyde, etc. Available technologies at commercial scale to address the CO separation are based on cryogenic distillation, liquid absorption, and adsorption processes. Nevertheless, if nitrogen is present in the gas mixture, the use of an absorption process may be considered as the most attractive technology at medium scale given that cryogenic distillation becomes less efficient with increasing N_2 content and pressure swing adsorption process has a lower yield [1]. Nowadays, the CO absorption process is based on the complexation/decomplexation reaction between CO and copper(I) aluminum chloride salt (CuAlCl_4) dissolved in an aromatic hydrocarbon, usually toluene, and has several concerns regarding the solubility of the complexing salt and its long-term activity. In this work, a novel approach to the separation and purification of CO is explored taking advantage of the outstanding properties offered by ionic liquids, namely, their negligible vapour pressure, high solvent capacity, wide liquid range and thermal and chemical stability.
机译:1.当进行烃的部分燃烧时,例如,当进行碳氢化合物的部分燃烧时,在工业过程的废气流中常被释放。炭黑制造,钢制造和碳化硅工艺。可以寻求该CO的选择性回收和储存作为获得有价值的副产物,例如氢或化学物质的方法。商业规模的甲醇,甲醛等可用于解决CO分离的技术基于低温蒸馏,液体吸收和吸附过程。然而,如果在气体混合物中存在氮气,则可以将吸收过程的使用视为中等规模中最吸引力的技术,因为随着N_2含量的增加,低温蒸馏变得较低,并且压力摆动过程具有较低的产量[1 ]。如今,CO吸收过程基于溶解在芳烃中的CO和铜(I)氯化铝盐(Cualcl_4)之间的络合/解用反应,通常是甲苯,并且对络合盐的溶解性有几个问题-term活动。在这项工作中,探讨了一种新的分离和纯化的方法,利用离子液体提供的优异性能,即它们可忽略的蒸气压,高溶剂容量,宽液体范围和热和化学稳定性。

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