Binary mixtures of choline chloride-based deep eutectic solvents as green extractants for the extraction of benzene from n-hexane

IF 0.125
Mohammed Awwalu Usman, Olumide Kayode Fagoroye, Toluwalase Olufunmilayo Ajayi, Abiola John Kehinde
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引用次数: 4

Abstract

A suitable green solvent for extraction of aromatics from aliphatics must possess good solvation and physicochemical properties, a rare occurrence in a single deep eutectic solvent (DES). Mixture of DESs could enable synergy and provide a good candidate extractant. In this study, DESs of glyceline, ethaline, and reline were synthesized and their binary mixtures (glyceline/ethaline, reline/ethaline, and glyceline/reline) produced by blending in various volume proportions. Twelve of such mixed solvents were prepared and their extraction efficiency for separating benzene from n-hexane investigated in a batch equilibrium process. Liquid–liquid equilibria (LLE) data for the pseudo-ternary systems of n-hexane + benzene + mixed DESs were measured at 303 K and 101.3 kPa. The distribution coefficient (D) and selectivity (S) of each pseudo-ternary system were determined to elicit extraction efficiency. The physicochemical properties of the mixed DESs were also measured. The results show that generally the distribution coefficients, selectivities, and physicochemical properties of the mixed DESs lie between the corresponding values for the constituent DES. The best performance was given by the mixed solvent of glyceline and ethaline in the 80:20 volume ratio, respectively, with D = 0.75 and S = 422.485. This assertion was further corroborated by higher percent recovery of benzene obtained from the said mixed DES (57.88%) relative to other mixed DESs (≤ 49.11%) examined in this study. Furthermore, its separation efficiency is superior to sulfolane but lower than glyceline, though there was a 9.4% reduction in its viscosity relative to glyceline.

以氯化胆碱为基础的二元共晶溶剂作为绿色萃取剂萃取正己烷中苯
一种适合从脂肪族中提取芳烃的绿色溶剂必须具有良好的溶剂化和理化性质,这在单一的深共晶溶剂(DES)中是罕见的。DESs混合物具有协同作用,是一种很好的萃取剂。在本研究中,合成了甘油、乙炔和线的DESs,并以不同的体积比例共混得到了它们的二元混合物(甘油/乙炔、线/乙炔、甘油/线)。制备了12种混合溶剂,并在间歇平衡过程中考察了它们对苯和正己烷的萃取效率。在303 K和101.3 kPa下,测定了正己烷+苯+混合DESs伪三元体系的液液平衡(LLE)数据。测定各伪三元体系的分布系数(D)和选择性(S),得出萃取效率。测定了混合DESs的理化性质。结果表明,混合DES的分布系数、选择性和理化性质均在各组分DES的对应值之间,其中以80:20体积比的甘油和乙炔混合溶剂为最佳,D = 0.75, S = 422.485。与本研究中检测的其他混合DES(≤49.11%)相比,从该混合DES中获得的苯回收率更高(57.88%),进一步证实了这一说法。此外,其分离效率优于亚砜,但低于甘氨酸,但其粘度相对甘氨酸降低了9.4%。
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来源期刊
Applied Petrochemical Research
Applied Petrochemical Research ENGINEERING, CHEMICAL-
自引率
0.00%
发文量
0
审稿时长
13 weeks
期刊介绍: Applied Petrochemical Research is a quarterly Open Access journal supported by King Abdulaziz City for Science and Technology and all the manuscripts are single-blind peer-reviewed for scientific quality and acceptance. The article-processing charge (APC) for all authors is covered by KACST. Publication of original applied research on all aspects of the petrochemical industry focusing on new and smart technologies that allow the production of value-added end products in a cost-effective way. Topics of interest include: • Review of Petrochemical Processes • Reaction Engineering • Design • Catalysis • Pilot Plant and Production Studies • Synthesis As Applied to any of the following aspects of Petrochemical Research: -Feedstock Petrochemicals: Ethylene Production, Propylene Production, Butylene Production, Aromatics Production (Benzene, Toluene, Xylene etc...), Oxygenate Production (Methanol, Ethanol, Propanol etc…), Paraffins and Waxes. -Petrochemical Refining Processes: Cracking (Steam Cracking, Hydrocracking, Fluid Catalytic Cracking), Reforming and Aromatisation, Isomerisation Processes, Dimerization and Polymerization, Aromatic Alkylation, Oxidation Processes, Hydrogenation and Dehydrogenation. -Products: Polymers and Plastics, Lubricants, Speciality and Fine Chemicals (Adhesives, Fragrances, Flavours etc...), Fibres, Pharmaceuticals.
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