JOURNAL OF CHEMICAL THERMODYNAMICS
·
2020
·
IF 2.888
Shihua Dong,Weizhen Sun,Yueyang Jiang,Bing Jia
Liquid-liquid equilibrium (LLE) data for {water + furfuryl alcohol + solvent (isopropyl ether, tert-butyl methyl ether, dichloromethane and methyl isobutylcarbinol)} ternary systems were determined at T = 298.2 K and p = 101.3 kPa. The distribution coefficients and separation factors were evaluated and the results showed that those solvents can effectively for furfuryl alcohol recovery from aqueous solutions. The Othmer-Tobias, Bachman and Hand equations were employed to validate the reliability of the experimental LLE data. Additionally, the experimental LLE data were correlated using the NRTL and UNIQUAC models and the binary interaction parameters were optimized. The root mean square deviations (RMSD) between the correlated data by NRTL and UNIQUAC models and the experimental LLE data were less than 0.36%, which demonstrated that both models can correlate experimental LLE data successfully.
研究领域:
化学工程
·
热力学
✓ 已验证
DOI
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2011
·
IF 2.089
Hengde Li,Tianfei Zhang,Weiqin Fu,Kazuhiro Tamura
Liquid–liquid equilibrium (LLE) data of the binodal curves and tie-line compositions were examined for ternary mixtures of (water + methanol + geraniol) and (water + ethanol + geraniol) at T = (283.15, 298.15, and 313.15) K. The immiscible area of the (water + methanol + geraniol) system is wider than that for the ethanol system at the same temperature. The experimental liquid–liquid equilibrium data have been represented by using the original UNIQUAC, extended UNIQUAC, and modified UNIQUAC models.
研究领域:
化学工程
·
物理化学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2014
·
IF 2.045
Fuqiong Lei,Qinbo Wang,Xing Gong,Binwei Shen,Wenming Zhang,Qing Han
The solubilities of succinic acid in acetic acid + water solvent mixtures at (303.2 to 333.2) K and acetic acid + cyclohexane solvent mixtures at (303.2 to 343.2) K were determined. It was found that the solubility of succinic acid in acetic acid + cyclohexane mixtures increases with increasing mass fraction of acetic acid at constant temperature. However, for the system of acetic acid + water solvent mixtures, acetic acid with the mass fraction of 0.20 shows the best dissolving capacity for succinic acid. The experimental data were well-correlated with universal quasi-chemical (UNIQUAC) equations, and the solubilities calculated by the model were in good agreement with experimental data.
研究领域:
物理化学
·
材料科学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2020
·
IF 2.369
Weibin Cai,Tiankun Liu,Hong Ye,Meng Chen,Xue Cheng
The ternary liquid–liquid equilibrium (LLE) data for cyclohexanone (CYC) + phenol + water were determined at T = (298.15, 313.15, and 323.15) K and atmospheric pressure. The distribution coefficients and separation factors were determined by the measured tie-line data, which showed the excellent performance of CYC in the extraction of phenol from aqueous solution. The reliability of LLE data was ascertained by the Bachman and Hand equations. The experimental data of the investigated ternary system were accurately correlated by the nonrandom two-liquid (NRTL) model and the universal quasi-chemical (UNIQUAC) model, and the relevant binary interaction parameters were calculated. For the NRTL and UNIQUAC models, the root-mean-square deviation values were lower than 0.6%.
研究领域:
化学工程
·
物理化学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2019
·
IF 2.298
Xiaoda Wang,Yuan Gao,Chaoqun Li,Zhixian Huang,Ting Qiu
Liquid–liquid equilibrium data were determined for the two ternary systems of water + thioglycolic acid (TGA) + 2-ethyl-1-hexyl thioglycolate (ETE) and water + 2-ethyl-1-hexyl thioglycolate (ETE) + 2-ethyl-1-hexanol (EHL) at 293.15, 303.15, and 313.15 K under 101 kPa. The nonrandom two-liquid (NRTL) and universal quasi-chemical (UNIQUAC) activity coefficient models were used to correlate the experimental LLE data. The LLE data calculated by the NRTL and UNIQUAC models were in good agreement with the experimental ones.
研究领域:
化学工程
·
物理化学
✓ 已验证
DOI
高影响因子
FLUID PHASE EQUILIBRIA
·
2015
·
IF 2.2
Yinchuan Pei,Qinbo Wang,Xing Gong,Fuqiong Lei,Binwei Shen
Liquid–liquid equilibrium (LLE) data for ternary systems water + cyclohexane + cyclohexanol and water + cyclohexane + cyclohexanone were measured at (303.2–333.2) K and under atmospheric pressure. The reliability of the experimental tie-line data was checked by the empirical Othmer–Tobias correlation. The distribution coefficient and separation factor were used to investigate the distribution of cyclohexanol and cyclohexanone between water and cyclohexane. The results show that the distribution coefficient of cyclohexanol or cyclohexanone between organic and aqueous phases increases with the increasing content of cyclohexanol or cyclohexanone in water, and so does it with the increasing of temperature. By using the NRTL and UNIQUAC activity coefficient models, the experimentally determined LLE data, along with the LLE data for another ternary system water + cyclohexanol + cyclohexanone [G. Xing, W. Qinbo, L. Fuqiong, S. Binwei, J. Chem. Eng. Data 59 (2013) 1651–1655], were correlated simultaneously. Good agreements were obtained between the correlated and experimentally determined tie-line data. The binary NRTL and UNIQUAC interaction parameters were obtained. Furthermore, four sets of quaternary LLE data for water + cyclohexane + cyclohexanol + cyclohexanone were experimentally determined at 318.2 K. The experimentally determined quaternary LLE data were compared with the NRTL model predicted LLE data, and generally agreements were obtained. It further verifies the reliability of the obtained binary model parameters, and indicates the obtained parameters could be used for prediction, as well as design and optimization of the related separation process.
研究领域:
化学工程
·
物理化学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2014
·
IF 2.045
Wenjie Cong,Qiuxiang Yin,Junbo Gong,Ying Bao,Meijing Zhang,Hongxun Hao,Baohong Hou,Yuhong Guo,Chuang Xie
Ternary phase diagram data of 1,2-dihydroacenaphthylene-dibenzofuran mixtures in a series of alcohols, including methanol, ethanol, propan-2-ol, propan-1-ol, butan-1-ol, and pentan-1-ol were measured using a dynamic method at 308.15 and 313.15 K. The experimental data were correlated with the Wilson model (including pseudobinary systems), UNIQUAC model, and NRTL model. The results indicate that pseudobinary systems with the Wilson equation give a better description of the solubility of the ternary system. The eutectic point shifts toward dibenzofuran when the more polar methanol and ethanol are used. This shift may help achieve a more efficient separation of 1,2-dihydroacenaphthylene and dibenzofuran.
研究领域:
化学工程
·
物理化学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF CHEMICAL THERMODYNAMICS
·
2018
·
IF 2.631
Qingsong Li,Bing Jia,Liping Wang,Mengmeng Yan,Hai Liu,Yingmin Yu
The liquid-liquid equilibrium (LLE) data for the water + 2,2,3,3-tetrafluoro-1-propanol + isopropyl ether/tert-butyl methyl ether ternary systems were measured at 298.2 K and 308.2 K under 101.3 kPa. The distribution coefficients and separation factors were employed to assess the capacity of solvents to extract 2,2,3,3-tetrafluoro-1-propanol from aqueous solution. Meanwhile, the reliability of the experimental data was confirmed using the Bachman and Hand equations. The NRTL and UNIQUAC models were used to correlate the experimental data and relevant binary interaction parameters were regressed. The root mean square deviations (RMSD) of the NRTL and the UNIQUAC models were less than 0.5%, which indicate that the experimental LLE data can be successfully correlated by both models.
研究领域:
化学工程
·
热力学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY
·
2019
·Vol. 96
·期 8
·955-965
·
IF 1.72
Jiaojiao Fang,Ting Zheng,Zhenyu Wu,Lihang Wu,Qinglong Xie,Fan Xia,Meizhen Lu,Yong Nie,Jianbing Ji
Epoxidized oils are eco-friendly plasticizers, which are industrially produced through the epoxidation reaction in a formic acid-hydrogen peroxide autocatalyzed system. The fundamental knowledge to describe the phase equilibrium of systems after epoxidation reaction is lacking, which is crucial for the design of the purification facilities. This work reported experimental data for the liquid–liquid equilibrium of three systems, i.e., epoxidized fatty acid methyl esters + formic acid + water, epoxidized fatty acid 2-ethylhexyl esters + formic acid + water, and epoxidized soybean oil + formic acid + water, in the temperature range (303.15–348.15) K under atmospheric pressure. The results indicated that the liquid–liquid equilibrium constant of formic acid in the systems followed the order of epoxidized fatty acid 2-ethylhexyl esters > epoxidized fatty acid methyl esters > epoxidized soybean oil. Moreover, the obtained experimental data were correlated using nonrandom two liquid (NRTL) and universal quasi chemical (UNIQUAC) models. The maximum root mean square deviation (RMSD) values as low as 0.0052 and 0.0263 were estimated using the NRTL and UNIQUAC model, respectively. The NRTL model is more suitable than the UNIQUAC model to describe the liquid–liquid equilibrium behavior of these ternary systems.
研究领域:
化学工程
·
环境科学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2019
·
IF 2.298
Wenyang Fan,Houchun Yan,Xin Huang,Zhaohui Liao,Qingsong Li,Zhanhua Ma
The extraction process as a kind of energy-saving and environmental protection technology can be used to separate phenols from low-temperature coal tar. The liquid–liquid equilibrium (LLE) data regarding ternary systems n-heptane + phenols + furfural were determined experimentally at 303.2, 323.2, and 343.2 K under the atmospheric pressure condition, where phenols refer to phenol, p-cresol, and 2,6-xylenol. The solvent extraction capacity was assessed by the solute distribution coefficient and selectivity. Othmer–Tobias and Bachman equations were utilized to validate the consistency of the measured data, which the linear correlation (R2) ≥ 0.99. Experimental LLE data were correlated utilizing the NRTL and UNIQUAC thermodynamic models with all of the RMSD and AARD values below 0.01, meaning that each ternary system is satisfactorily in agreement at temperatures studied and the NRTL model gives better agreement than the UNIQUAC model for ternary systems.
研究领域:
化学工程
·
热力学
✓ 已验证
产品关联
DOI
高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2014
·
IF 2.045
Yao Chen,Xiaoming Zhou,Caiyu Wen,Cui Wang,Jitai Guo
Tie lines were investigated for two quaternary systems of water + ethanol + diethyl carbonate + methylbenzene or heptane and three related ternary systems of water + diethyl carbonate + ethanol or methylbenzene or heptane at 303.15 K and atmospheric pressure. The raw experimental tie line data were correlated using the modified and extended UNIQUAC activity coefficient models. The reliability of the experimental tie line data was tested with the Othmer–Tobias equation. Distribution coefficients were calculated from the experimental tie line data to analyze the solubility of components in aqueous and organic phases.
研究领域:
化学工程
·
物理化学
✓ 已验证
产品关联
DOI
高影响因子
FLUID PHASE EQUILIBRIA
·
2014
·
IF 2.241
Hao Li,Shuqian Xia,Peisheng Ma,Fangyou Yan,Zhen Yang,Yang Li
Bio-oil, derived from biomass flash pyrolysis, has been recognized as an important renewable resource for resolving the current energy crisis. However, the pyrolysis oil consists of complicated composition and has some undesired properties, including acidity, relatively high viscosity, limited thermal stability, low heating value, which hinder the direct application of bio-oil. So, separation and purification of the pyrolysis oil are important and the phase equilibrium data of the bio-fuel related mixtures is essential for the design and simulation of the processes. In this context, isobaric vapor–liquid equilibrium (VLE) data for the three binary mixtures in the pyrolysis oil, toluene + anisole, n-butylbenzene + anisole, and guaiacol + anisole, have been measured at 101.33 kPa by a modified Rose–Williams still. All of the experimental VLE data were checked by the Herington analysis method and were verified the thermodynamic consistency. No azeotropic behavior was observed in the three binary systems. The measured data were well correlated by the non-random two-liquid (NRTL), universal quasi-chemical activity coefficient (UNIQUAC), and Wilson model, respectively. The corresponding parameters for the three models were obtained. The average absolute deviations of the temperature and the vapor compositions correlated by the three models for all the systems are below 0.55 K and 0.019, respectively.
研究领域:
化学工程
·
可再生能源
✓ 已验证
产品关联
DOI
高影响因子
危险品化学品经营许可证（带存储）