首页> 外文期刊>The Journal of Chemical Thermodynamics >Removal of 2-and 3-methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents
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Removal of 2-and 3-methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents

机译:使用基于四氧基溴化铵的深共晶溶剂作为萃取脱硫剂,从它们的与正庚烷中除去2-和3-甲基噻吩。作为萃取脱硫剂

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Deep eutectic solvents (DESs) have previously been proven to be potential extractive desulfurization agents. However, so far, only the recovery of thiophene, benzothiophene and dibenzothiophene from aliphatic mixtures have been assessed. In this work, two other sulfur-containing hydrocarbons (i.e., 2-methylthiophene and 3-methylthiophene) were for the first time recovered from their mixtures with n-heptane using two DESs as extracting agents: (i) tetrahexylammonium bromide: ethylene glycol with molar ratio 1:2 (DES 1) and (ii) tetrahexylammonium bromide: glycerol with molar ratio1:2 (DES 2). First, the binary solubilities of n-heptane and 2- and 3-methylthiophene in both DESs at 298 K and atmospheric pressure were measured. Thereafter, the liquid-liquid equilibrium (LLE) data for the four pseudo-ternary systems consisting of n-heptane + 2-methylthiophene/3-methylthiophene + DES 1/DES 2 were determined at 298 K and atmospheric pressure. On the basis of the experimental data, the distribution ratios and selectivities were calculated and used to determine the viability of both DESs for the industrial extractive desulfurization process. The experimental data were also succesfully correlated using the non-random two-liquid (NRTL) model. Both DESs were found to be able to extract 2- and 3-methylthiophene from n-heptane, with DES 1 being more preferable over DES 2. (C) 2018 Elsevier Ltd.
机译:先前已被证明是潜在的萃取脱硫剂的深度共晶溶剂。然而,到目前为止,已经评估了噻吩,苯并噻吩和二苯噻吩的回收率已经评估了来自脂族混合物的回收率。在这项工作中,使用两种其他含硫烃(即,2-甲基噻吩和3-甲基噻吩)使用两个DES作为提取剂的二甲烷作为萃取剂的二庚烷回收它们的混合物:(i)四氧基溴化物:乙二醇摩尔比1:2(DES 1)和(II)四氧基溴化铵:具有摩尔比例的甘油,1:2(DES 2)。首先,测量二庚烷和2-甲基噻吩的二元溶解度在298k和大气压下进行。此后,在298k和大气压下测定由正庚烷+ 2-甲基噻吩/ 3-甲基噻吩+ des1 / des 2组成的四个伪三元系统的液体平衡(LLE)数据。在实验数据的基础上,计算分配比率和选择性,并用于确定DES的生存能力用于工业萃取脱硫过程。使用非随机双液(NRTL)模型也成功地相关。发现两个DES都能够从正庚烷中提取2-甲基噻吩,更优选在DES 2.(c)2018 Elsever Ltd.

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