JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2019
·
IF 2.298
Yong-Sheng Xu,Xin Liu,Kang-Kang Pei,Rui-Xiong Zhao,Guo-Liang Zhang,Qing Xia,Feng-Bao Zhang
The solubilities of naphthalene in decalin, octane, dodecane, dichloromethane, trichloromethane, carbon tetrachloride, 1,2-dichloroethane, o-dichlorobenzene, 1-octanol, 2-octanone, 4-methyl-2-pentanone, and benzene were measured by a dynamic method over the temperature range of 279 to 330 K at atmospheric pressure. By comparison, the experimental results indicated that the molality solubility in dichloromethane reached maximum at certain temperature. Then, the Apelblat equation, the λh equation, the Wilson equation, and the nonrandom two liquid (NRTL) equation were used to correlate the experimental data. The NRTL equation was regarded as the effective model for all the solvents. Finally, the mixing properties were also calculated based on the NRTL equation. All these data were particularly instructive for the process of recycling naphthalene.
研究领域:
物理化学
·
化工过程
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DOI
高影响因子
JOURNAL OF CHEMICAL THERMODYNAMICS
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2014
·
IF 2.423
Hui Wang,Qinbo Wang,Zhenhua Xiong,Chuxiong Chen,Binwei Shen
The solubility of benzoic acid in binary (benzyl alcohol + benzaldehyde) solvent mixtures was measured at temperature from (298.35 to 355.65) K and atmospheric pressure. The measured solubility increases with the increasing temperature at constant solvent composition. The effects of mass fraction benzaldehyde in the solvent mixtures at (0.0 to 1.00) on the solubility were studied. The measured solubility decreases with the increasing mass fraction of benzaldehyde. The experimental results were correlated with the non-random two-liquid (NRTL) equations, and good agreement between the correlated and the experimental values was obtained. Thermodynamic functions for the solution of benzoic acid in binary (benzyl alcohol + benzaldehyde) solvent mixtures were calculated with the van’t Hoff plot. The apparent dissolution Gibbs free energy change was also calculated.
研究领域:
物理化学
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热力学
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产品关联
DOI
高影响因子
ACS Omega
·
2025
·
IF 4.3
Zixi Wu,Chunxiang Huang,Leyi Li,Jinxiang Cao,Yingjie Liu,Qing Ye,Jinlong Li
The paper presents experimentally determined solubility results of lithium bromide in ionic liquid + water and assesses the effect of the addition of ionic liquids (ILs) on the solubility of lithium bromide (LiBr) in water. The solubility of LiBr in pure water has been determined and compared to the literature data. It is known that LiBr aqueous solutions are widely used as working fluids in low-temperature thermal energy recovery systems. However, the aqueous LiBr solution is easy to crystallize, which could cause equipment corrosion. One of the possibilities for improving the properties of the H2O/LiBr refrigerant system is the use of an additive to increase the solubility of LiBr in water. Three ILs were selected as an additive: 1-ethyl-3-methylimidazolium acetate ([EMIM][OAc]), 1-ethyl-3-methylimidazolium bromide ([EMIM]Br), and 1-butyl-3-methylimidazolium bromide ([BMIM]Br). In this study, new empirical parameters for the calculation of LiBr solubility in water were provided. A reasonable prediction of phase equilibrium data is made using the COSMO-SAC model. The NRTL equation is also calculated. The maximum deviation of COSMO-SAC is 7.56%, and the deviation of the other calculations is less than 2%. These experimental and theoretical findings offer valuable insights into the selection and optimization of working fluids in absorption cycle systems.
研究领域:
化学工程
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热力学
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材料科学
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物理化学
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产品关联
DOI
PubMed
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2017
·
IF 2.323
Shenfeng Yuan,Jiafeng Liu,Hong Yin,Zhirong Chen
Liquid–liquid equilibrium (LLE) data for the quaternary systems of ethanol + butanol + octane + water and ethanol + butanol + nonane + water were obtained at 298.15 K under atmospheric pressure in this article. The nonrandom two-liquid (NRTL) equation was used to correlate the LLE data, and the two quaternary systems were used to regress the interaction parameters of the model. The obtained interaction parameters of NRTL model were used to predict the LLE of the quinary system ethanol + butanol + octane + nonane + water and was compared with the experimental values. The results showed that the calculated values coincided with the experimental data well, an indication that the NRTL model and the interaction parameters obtained from quaternary systems could be used to predict the LLE data of quinary system. The LLE data of the quinary system were also characterized by the distribution coefficient and the selectivity, and the results showed that the ethanol aqueous solution which contained about 40 wt % ethanol was suitable for separating butanol from the butanol–octane–nonane mixture.
研究领域:
化学工程
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热力学
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物理化学
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产品关联
DOI
高影响因子
CHEMICAL PAPERS
·
2016
·Vol. 70
·期 5
·585-593
·
IF 1.326
Lin Zhu,Fang-Fang Li,Ji-Qin Zhu,Zhi-Gang Lei
Olefins and paraffins are important basic chemical raw materials with so similar molecular structure and volatility that their separation is a difficult and energy-consuming process. Liquid–liquid equilibrium (LLE) data were determined for ternary systems of: 1-hexene + hexane + solvent at 25°C, 30°C, and 35°C, and N-formylmorpholine (NFM), N-methyl-2-pyrrolidone (NMP), 7-butyrolactone (GBL), and 1-methylimidazole (1-MEI) as the solvents studied. Liquid–liquid equilibrium data for each system were correlated to the NRTL (Non-Random Two Liquid) equation and the interaction parameters presented. The calculated results agree well with the experimental data.
研究领域:
化学工程
·
物理化学
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DOI
高影响因子
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