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首页> 外文期刊>Separation and Purification Technology >Towards the potential of trihexyltetradecylphosphonium indazolide with aprotic heterocyclic ionic liquid as an efficient absorbent for membrane-assisted gas absorption technique for acid gas removal applications
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Towards the potential of trihexyltetradecylphosphonium indazolide with aprotic heterocyclic ionic liquid as an efficient absorbent for membrane-assisted gas absorption technique for acid gas removal applications

机译:朝向Trihexyltexyltexylonium indazoLide用非质子杂环离子液体作为酸性气体去除应用的膜辅助气体吸收技术的有效吸收剂的潜力

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摘要

The present study deals with complex experimental evaluation of a unique hybrid technique - membrane assisted gas absorption, which is proposed as an alternative approach to natural gas sweetening, and explores the ionic liquid with aprotic heterocyclic anion - trihexyltetradecylphosphonium indazolide as a component of the combined absorbent system. The synthesized ionic liquid was analyzed by C-13 and H-1 NMR in order to validate its formation and structure, afterwards the physicochemical properties, namely, density, viscosity, and absorption loading with respect to CH4, CO2 and H2S were determined, as well as the mass transfer properties of the combined membrane-absorbent system (permeability, diffusivity and sorption coefficients). The trihexyltetradecylphosphonium indazolide characterized by almost equimolar absorption loading for CO2 at elevated pressure, and the combined membrane-absorbent system provides selectivity up to 62 and 106.9 for the CH4/CO2 and CH4/H2S pairs respectively. Further, the efficiency of the proposed technique was evaluated experimentally on the example of separation of two binary CH4-based mixtures with CO2 and H2S as impurities. As a result of treatment, the purified product stream contains up to 93.34 and 99.998 vol% of CH4 in the case of CO2 and H2S removal, respectively.
机译:本研究对一种独特的混合技术——膜辅助气体吸收进行了复杂的实验评估,该技术被提议作为天然气脱臭的替代方法,并探索了含有非质子杂环阴离子的离子液体——三己基十四烷基膦吲唑内酯,作为组合吸附系统的一个组成部分。通过C-13和H-1 NMR对合成的离子液体进行分析,以验证其形成和结构,然后测定其物理化学性质,即密度、粘度和对CH4、CO2和H2S的吸收负荷,以及组合膜吸收系统的传质特性(渗透性、扩散性和吸附系数)。三己基十四烷基膦吲唑内酯在高压下对CO2的吸附量几乎为等摩尔,组合膜吸收系统对CH4/CO2和CH4/H2S的选择性分别高达62和106.9。此外,以分离以CO2和H2S为杂质的两种二元CH4基混合物为例,对所提出技术的效率进行了实验评估。经过处理后,在去除CO2和H2S的情况下,净化后的产品流中CH4的体积分数分别高达93.34%和99.998%。

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