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首页> 外文期刊>Fluid Phase Equilibria >Oil desulfurization using deep eutectic solvents as sustainable and economical extractants via liquid-liquid extraction: Experimental and PC-SAFT predictions
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Oil desulfurization using deep eutectic solvents as sustainable and economical extractants via liquid-liquid extraction: Experimental and PC-SAFT predictions

机译:通过液液提取使用深层共晶溶剂的油脱硫:实验和PC-Saft预测

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摘要

The reduction of the sulfur content in crude oil is of utmost importance in order to meet the stringent environmental regulations. Thiophene and its derivatives are considered key substances to be separated from the crude oil. In previous works, six deep eutectic solvents (DESs) based on tetraethylammonium chloride, tetrahexylammonium bromide and methyltriphenylphosphonium bromide as hydrogen bond acceptors (HBAs) and polyols (ethylene glycol and glycerol) as hydrogen bond donors (HBDs) were successfully applied for the extraction of thiophene from {n-alkane + thiophene} mixtures via liquid liquid extraction. One of the objectives of this work was to study the effect of the aliphatic hydrocarbon type length (e.g. n-hexane vs n-octane) on the extraction performance of the same DESs. Extraction performance was evaluated by the selectivity and the thiophene distribution coefficient. Based on new experimental data, higher selectivities and lower thiophene distribution coefficients were obtained when thiophene was extracted from n-octane instead of n-hexane. Another objective was to predict the phase behavior of the ternary systems {n-alkane + thiophene + DES) using Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT). The PC-SAFT "pseudo-pure component" approach was applied, in which a DES was considered as a pseudo-pure compound (not a mixture). The pure-component parameters of the DESs were obtained by fitting to liquid density data, which were measured at temperatures between 298.2 K and 323.2 K. Binary interaction parameters were fitted to experimental binary LLE data for the systems {n-alkane + DES) and {thiophene + DES) at 298.2 K and atmospheric pressure, while the LLE data of the ternary systems {n-alkane + thiophene + DES) were fully predicted. It was found that the distribution coefficients and selectivity of the ternary systems containing DESs could be qualitatively well predicted using this model. (C) 2018 Elsevier B.V. All rights reserved.
机译:原油中硫含量的降低至关重要,以满足严格的环境法规。噻吩及其衍生物被认为是与原油分离的关键物质。在以前的作用中,成功地应用于氢粘合剂受体(HBA)和多元醇(乙二醇)和多元醇(乙二醇)和多元醇(乙二醇)作为氢键供体(HBDS)的六种深层共晶溶剂(DES)作为氢粘合剂受体(HBA)和多元醇(乙二醇)。噻吩来自{N-烷烃+噻吩}通过液态液萃取混合物。这项工作的目的之一是研究脂族烃类长度(例如正己烷Vs n-辛烷值)对同一DES的提取性能的影响。通过选择性和噻吩分布系数评估提取性能。基于新的实验数据,当从N-辛烷烯烯烃代替正己烷时,获得更高的选择性和降低噻吩分布系数。另一个目的是使用扰动链统计关联流体理论(PC-Saft)预测三元体系{N-烷烃+噻吩+ des)的相行为。施加PC-SAFT“假纯组分”方法,其中将DES被认为是伪纯化合物(不是混合物)。通过拟合到液体密度数据获得DES的纯组分参数,其在298.2k和323.2k的温度下测量。二元相互作用参数适用于系统的实验二进制LLE数据(N-alkane + des)和{Thiophene + DES)在298.2 k和大气压下,而全部预测三元体系的lex数据{N-烷烃+噻吩+ des)。发现,使用该模型可以定性地预先预测包含DES的三元系统的分布系数和选择性。 (c)2018 Elsevier B.v.保留所有权利。

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