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首页> 外文期刊>Journal of Molecular Liquids >Choline chloride-based deep eutectic solvents as green extractant for the efficient extraction of 1-butanol or 2-butanol from azeotropic n-heptane plus butanol mixtures
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Choline chloride-based deep eutectic solvents as green extractant for the efficient extraction of 1-butanol or 2-butanol from azeotropic n-heptane plus butanol mixtures

机译:基于氯化胆碱基的深对共晶溶剂作为绿色萃取剂,用于从共沸的N-庚烷加丁醇混合物中有效提取1-丁醇或2-丁醇的萃取剂

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摘要

In this study, choline chloride-based deep eutectic solvents are used as green extractant for the efficient extraction of 1-butanol or 2-butanol from azeotropic n-heptane + butanol mixtures at 298.15 K and atmospheric pressure. Choline chloride as hydrogen bond acceptor (HBA) is mixed with urea, ethylene glycol, glycerol, and 1,2-propanediol (propylene glycol) as hydrogen bond donors (HBDs) to study the effect of different choline chloride-based deep eutectic solvents on the extraction efficiency. The obtained results show that, although all the DESs provide solute distribution ratios smaller than unity (beta < 1), the measured experimental selectivity values are much higher than unity (S> > 1), which is of interest for the economic feasibility of industrial extraction operations. The extraction capacity of the studied deep eutectic solvents for the separation of n-heptane +1-butanol mixture is compared with seven commonly used imidazolium-based ionic liquids. The experimental results are compared to UNIQUAC Functional-group Activity Coefficients (UNIFAC) model. It is visually observed that UNIFAC model predicts satisfactorily the equilibrium tie-lines, where the root-mean-square deviation (RMSD) for extraction of 1-butanol by ChCl-urea, ChCl-ethylene glycol, ChCl-glycerol and ChCl-1,2-propanediol are 2.99, 4.38, 1.12, and 1.56, respectively. In the case of 2-butanol extraction using the mentioned DESs, the RMSD is 0.69, 3.13, 1.47, and 1.11, respectively. (C) 2020 Elsevier B.V. All rights reserved.
机译:在这项研究中,胆碱氯化物系共晶深溶剂用作298.15ķ绿色萃取剂为1-丁醇或从共沸正庚烷+丁醇的混合物2-丁醇的有效提取和大气压力。氯化胆碱作为氢键受体(HBA)与尿素,乙二醇,丙三醇,和1,2-丙二醇(丙二醇)作为氢键供体(HBDS)混合来研究不同胆碱的作用氯化物系共晶深上的溶剂提取效率。将所得到的结果表明,尽管所有的DESS提供溶质分布比率小于1(测试版<1),测得的实验选择性值比统一高得多的(S 1),这是令人感兴趣用于工业的经济可行性提取业务。所研究的低共熔深的溶剂为正 - 庚烷的分离的提取容量+ 1-丁醇混合物与7常用的基于咪唑鎓的离子液体相比。实验结果进行比较,以UNIQUAC官能团的活度系数(UNIFAC)模型。据视觉上观察到,UNIFAC模型预测令人满意的平衡结线,其中对于由氯仿 - 脲萃取1-丁醇的根均方偏差(RMSD),氯仿 - 乙二醇,CHCL-甘油和CHCl-1, 1,2-丙二醇是2.99,4.38,1.12,和1.56,分别。在使用上述的DESS 2-丁醇萃取的情况下,RMSD为0.69,3.13,1.47,和1.11,分别。 (c)2020 Elsevier B.v.保留所有权利。

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