Thermophysical properties of 1-ethyl-3-methylimidazolium ethylsulfate + water binary mixtures between 283 and 343K: A feasible fluid for absorption refrigeration

Xavier Paredes , M.Soledade C.S. Santos , Luís C.S. Nobre , Miguel V.R. Silva , Ana R.P. Gonçalves , Carla S.G.P. Queirós , Carlos Nieto de Castro , Fernando J.V. Santos
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Abstract

Absorption-refrigeration cycles have been used for more than a century, and the most frequent refrigerant-absorbent working pairs are H2O-LiBr and NH3-H2O. The high coefficient of performance (COP) and affordability of these fluids still justifies their use, despite major drawbacks like the corrosion and crystallization risks, as well as limitations in terms of operating temperature and pressure for H2O-LiBr solutions, NH3 flammability and toxicity and use under high pressure, corrosiveness and alkalinity of its aqueous solutions, and the need of distillation solutions for NH3-H2O separation. Societal demands to reduce the environmental and health impact of chemicals used in industry, has led to the search for new systems for industrial applications. Recently, ILs emerged as absorbent candidates for absorption systems, due to their thermal stability, very low vapour pressure, and solvent capacity, which adds the possible use of their aqueous mixtures with low viscosity and toxicity, and significant COP values, making them excellent alternatives for new working absorbing pairs. From several ionic liquids proposed, 1-ethyl-3-methylimidazolium ethylsulfate, [C2mim] [EtSO4], is a good candidate, namely mixed with water. This low-toxicity ionic liquid was chosen to screen the reliability of available data on aqueous mixtures for the estimate of coefficient of performance (COP), targeting a potential application in absorption refrigeration cycles (ARC). The aqueous-rich mixtures (xIL < 0.1) present solution viscosities compatible with pumping devices used nowadays in refrigeration systems, and ensure enhanced wetting, affording improved heat transfer by conduction.
Several mixtures of pure ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate ([C2mim] [EtSO4]) with water were studied over the whole composition range, between 283.15 K and 343.15 K, at 0.1 MPa. Density, speed of sound, refractive index, viscosity, surface tension, and electrical conductivity were measured experimentally and compared with literature data. The experimental results are consistent with the evolvement of solution molecular structure with increasing water content previously predicted by MD simulations, evidencing a remarkable agreement of the notable transition points, and supporting previous studies in this laboratory with other ionic liquid aqueous systems, namely [C2mim] [CH3SO3] and [C2mim] [N(CN)2].

Abstract Image

283 ~ 343K间1-乙基-3-甲基咪唑硫酸乙酯+水二元混合物的热物理性质:一种可行的吸收式制冷流体
吸收-制冷循环已经使用了一个多世纪,最常见的制冷剂-吸收工作对是H2O-LiBr和NH3-H2O。尽管存在腐蚀和结晶风险、H2O-LiBr溶液的工作温度和压力、NH3的可燃性和毒性以及高压下使用、水溶液的腐蚀性和碱性以及NH3- h2o分离需要蒸馏溶液等方面的限制,但这些流体的高性能系数(COP)和价格低廉仍然值得使用。社会要求减少工业中使用的化学品对环境和健康的影响,这促使人们寻找新的工业应用系统。最近,由于其热稳定性、极低的蒸气压和溶剂容量,ILs成为吸收系统的吸收剂候选人,这增加了其低粘度和毒性的水混合物的可能用途,以及显著的COP值,使其成为新的工作吸收对的优秀替代品。从提出的几种离子液体中,1-乙基-3-甲基咪唑硫酸乙酯[C2mim] [EtSO4]是较好的候选离子液体,即与水混合。选择这种低毒性离子液体是为了筛选水性混合物中可用数据的可靠性,以估计性能系数(COP),目标是在吸收式制冷循环(ARC)中有潜在的应用。富水混合物(xIL <;0.1)目前的溶液粘度与目前在制冷系统中使用的泵送装置兼容,并确保增强润湿,通过传导提供更好的传热。研究了纯离子液体1-乙基-3-甲基咪唑硫酸乙酯([C2mim] [EtSO4])在283.15 K ~ 343.15 K、0.1 MPa下与水的混合物。实验测量了密度、声速、折射率、粘度、表面张力和电导率,并与文献数据进行了比较。实验结果与先前MD模拟预测的溶液分子结构随含水量增加的演变过程相一致,证明了显著的过渡点的显著一致性,并支持了本实验室先前对其他离子液体水体系(即[C2mim] [CH3SO3]和[C2mim] [N(CN)2])的研究。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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