JOURNAL OF CHEMICAL AND ENGINEERING DATA
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2023
·
IF 2.6
Jingwei Cao,Hongyue Guo,Qingsong Li
Ternary liquid–liquid phase equilibrium (LLE) data of water + 3-pentanone + extractants (methyl tert-butyl ether, 2-ethyl-1-hexanol, o-xylene, ethyl acetate) were measured to separate 3-pentanone of high purity from aqueous solutions at 308.2 K under 101.3 kPa. The ability to extract 3-pentanone from aqueous solutions was assessed by distribution coefficient (D) and separation factor (S). Hand and Bachman equations tested the reliability of the experimental data with linear coefficients (R2) not less than 0.99. Meanwhile, UNIQUAC and NRTL thermodynamic models regressed experimentally measured data to get the optimal binary interaction parameters, and the root mean square deviation (RMSD) was not more than 0.4%. The GUI-MATLAB program verified the consistency of binary parameters obtained from the NRTL model well.
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高影响因子
JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2023
·
IF 2.6
Fan Yang,Qinqin Zhang,Hua Xin,Tianzhao Wu,Zhigang Zhang
Separating the mixture of the target product n-propyl acetate (NPAC) and the unreacted reactant n-propanol (NPA) is necessary during the production of NPAC. NPA and NPAC cannot be separated by simple distillation because the two could form an azeotrope under atmospheric pressure. Liquid–liquid extraction is an energy-saving and environment-friendly method for separating azeotropic mixtures. Ionic liquids (ILs) are promising alternatives to conventional extractants for separating azeotropes due to the advantages of designability and negligible vapor pressure. In this study, the liquid–liquid equilibrium (LLE) data for the ternary systems of NPAC + NPA + 1-butyl-3-methylimidazolium dihydrogen phosphate ([BMIM][H2PO4]) or 1-butyl-3-methylimidazolium thiocyanate ([BMIM][SCN]) or 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIM][BF4]) were determined at 303.15 K and 101.3 kPa. The accuracy of the experimental LLE data was checked by the Bachman, Hand, and Othmer–Tobias equations. The selectivity and partition coefficient were calculated to evaluate the extraction capability of the selected extractants. The experimental LLE data were correlated with the nonrandom two-liquid model, and the binary interaction parameters were regressed. Finally, the separation mechanism of the three ILs was explored through σ-profile analysis.
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JOURNAL OF CHEMICAL AND ENGINEERING DATA
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2019
·
IF 2.298
Yuwen Fan,Wenjun Zhu,Yonghong Hu,Wenge Yang,Qiang Xu,Xinxin Liu,Bin Heng
In the study, the solubility of l-serine were measured in eight common pure solvents and binary mixed solvents (acetonitrile + water, isopropanol + water, methanol + water, and acetone + water) from 278.15 to 333.15 K under atmospheric pressure by gravimetric method (acetone was measured from 278.15 to 328.15 K). The solubility of l-serine increases with increasing temperature, and the order in eight common pure solvents is water > acetonitrile > methanol > acetone > ethyl acetate > ethanol > n-butanol > isopropanol. In binary mixed solvents, the solubility of l-serine is dependent on temperature and solvent composition. Also, the solubility of l-serine increases with increasing temperature, and it decreases as the concentration of acetonitrile, isopropanol, methanol, or acetone increases at a constant temperature. The experimental data in eight pure solvents were fitted by the modified Apelblat model, Buchowski–Ksiazaczak λh model. The modified Apelblat equation, combined nearly ideal binary solvent/Redlich–Kister (CNIBS/R–K) model, and Jouyban–Acree model were used to correlate the experimental data in four binary solvents. Among the four models, the modified Apelblat model is more suitable with a higher accuracy than the other three models. The experimental data can be used to optimize the industrial manufacturing process of l-serine.
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JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2019
·
IF 2.298
Xiaoqin Shi,Chenxu Li,Hui Guo,Shufeng Shen
Blends of amines with alkoxyethanols have been potentially used as alternative absorbents to conventional aqueous amines for energy-efficient CO2 capture, due to the lower specific heat capacity and enthalpy of vaporization of organic solvents than water. In this work, densities and viscosities were measured at atmospheric pressure for binary liquid mixtures of 2-(methylamino)ethanol (MAE) + 2-methoxyethanol (EGME), MAE + 2-ethoxyethanol (EGEE), and MAE + 2-butoxyethanol (EGBE) over the entire composition range and at temperatures of 293.15–353.15 K. The excess molar volume and viscosity deviations were also calculated and fitted by the Redlich–Kister equation. The calculated values of density and viscosity from the proposed correlations are in good agreement with the experimental values, with average absolute relative deviations within 0.06 and 1.23% for density and viscosity, respectively. The variations of excess or deviation properties with temperature and components were also discussed in terms of intermolecular interactions and structural effects.
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PHYSICS AND CHEMISTRY OF LIQUIDS
·
2019
·
IF 1.526
Mengsha Cai,Zhaoshan Liu,Haiyun Sun,Yongsheng Guo,Wenjun Fang
Densities (ρ) and viscosities (η) of a ternary system cyclopropanemethanol (1) + 2,2,4-trimethylpentane (2) + decalin (3) and three corresponding binary systems were measured at temperatures from 293.15 K to 323.15 K and atmospheric pressure. Densities were obtained by using a vibrating-tube densimeter. Viscosities were determined by an automatic microviscometer based on the rolling ball principle. The excess molar volumes (VmE) and viscosity deviations (Δη) of the ternary system were derived from the experimental data and then were fitted to Clibuka, Nagata–Tamura and Redlich–Kister equation, respectively. The binary subsystems were correlated by Redlich–Kister equation. The values of VmE and Δη were used to discuss the nature of mixing behaviours between mixture components.
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JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY
·
2018
·Vol. 135
·期 6
·3363-3373
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IF 2.209
Zhang Shijie,Zhang Jiaoqiang,Kou Kaichang,Jia Qian,Xu Yunlong,Zerraza Sofiane,Liu Ning,Hu Rongzu
2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexazisowurtzitane (HNIW)·1,3,5,7-tetranitro-1,3,5,7-tetrazocane (HMX) co-crystal in a 2:1 molar ratio was prepared by a solvent/non-solvent method, and the co-crystal has been characterized by several methods. The enthalpies of dissolution of 2HNIW·HMX co-crystal in N,N -dimethylformamide at different temperatures were measured by a DC08-1 Calvet microcalorimeter under standard atmospheric pressure, and it is indicated that the dissolutions are exothermic process. The empirical formulae for the calculation of the molar enthalpy ( \(\Delta_{\text{diss}} H\) ) of dissolution, relative partial molar enthalpy ( \(\Delta_{\text{diss}} H_{\text{partial}}\) ), relative apparent molar enthalpy ( \(\Delta_{\text{diss}} H_{\text{apparent}}\) ), and enthalpy of dilution ( \(\Delta_{\text{dil}} H_{1,2}\) ) at 298.15 K are obtained. The differential enthalpies ( \(\Delta_{\text{dif}} H\) ) and kinetic equations describing the dissolution process at different temperatures are deduced. Furthermore, the apparent activation energy E = 10.54 ± 0.22 kJ mol -1 and pre-exponential constant A = 0.34 ± 0.03 s −1 of 2HNIW·HMX co-crystal are obtained. The standard molar Gibbs free energy of activation ( \(\Delta G_{ \ne }^{\theta }\) ) at different temperatures is 86.44 ± 0.02 kJ mol −1 (298.15 K), 88.02 ± 0.03 kJ mol −1 (303.15 K), 89.61 ± 0.01 kJ mol −1 (308.15 K), 91.18 ± 0.01 kJ mol −1 (313.15 K), and 92.75 ± 0.02 kJ mol −1 (318.15 K), respectively. The standard molar entropy of activation ( \(\Delta S_{ \ne }^{\theta }\) ) and standard molar enthalpy of activation ( \(\Delta H_{ \ne }^{\theta }\) ) are − 262.55 ± 0.72 J mol −1 K −1 and 7.98 ± 0.22 kJ mol −1 , respectively.
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JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2016
·
IF 1.835
Ying Zhang,Xiong Zheng,Maogang He,Yutian Chen
Ethers are usually used as gasoline additives, and now 2-methoxy-2-methylpropane (MTBE) is the most widely used fuel additive. The speed of sound in MTBE with a specified mass purity higher than 0.990 (GC) was measured by the Brillouin light scattering method in the temperature range of 293.15–673.15 K and for pressures up to 10 MPa, including saturated liquid/vapor, liquid, and supercritical fluid. The correlations for the speed of sound in saturated liquid/vapor and liquid were proposed by employing the experimental results. Comparing the calculated results with the experimental data, the average absolute deviations are 0.50% for saturated liquid, 0.20% for saturated vapor, and 0.24% for liquid. The tendency of speed of sound to temperature and pressure was also analyzed.
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JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2016
·
IF 1.835
Xiaohong Han,Zhangzhang Yang,Zanjun Gao,Wenjie Guan,Guangming Chen
Fluoroethane (HFC-161) is one of the most promising alternative refrigerants because of its excellent environmental and thermodynamic properties. It was considered as one of the most promising absorption working fluids in the absorption refrigeration. To make a better application of the refrigerant in absorption refrigeration systems, suitable absorbents should be selected for matching HFC-161. Vapor–liquid equilibrium (VLE) data is the key of the chemical engineering simulation and the refrigeration cycle calculation. On the basis of these, the vapor–liquid equilibrium data for the mixture of HFC-161 + dimethyl ether triethylene glycol were obtained at temperatures from 293.15 to 353.15 K by using a recirculation apparatus. The VLE data were then correlated by the Peng−Robinson (PR) equation of state combined with the modified Huron-Vidal first order (MHV1) mixing rule and nonrandom two liquid (NRTL) model. The experimental results had a good consistency with calculated values. Phase behaviors of HFC-161 combined with different absorbents were compared in this paper.
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Journal of Materials Chemistry C
·
2016
·Vol. 4
·期 45
·10654-10663
·
IF 5.066
Longhui Zheng,Guozheng Liang,Aijuan Gu,Li Yuan,Qingbao Guan
High loading of ceramics has been the biggest shortcoming of fabricating high-k ceramic/polymer composites. Herein, unique pure barium titanate (BT) foams with three-dimensional interconnecting foam channels, coded as BTFs, were synthesized using a polymer foam replication method, and the BT content of foams is adjustable. In addition, various loadings of BTF were embodied into cyanate ester (CE) resin to develop a new kind of high-k composite. The spatial structure and content of BTF on the thermal and dielectric properties of BTF/CE composites were systematically researched, and compared with those of traditional composites based on commercial BT powders and ground BTF powders (BTFp), respectively. The results show that BTF/CE composites exhibit a much higher dielectric constant at very low concentrations of BTF than those of BT/CE and BTFp/CE composites. Typically, when the BTF content is as low as 33.5 vol%, the dielectric constant of the resultant BTF6(1200)/CE composite reaches 141.3 (100 Hz), about 8.4 and 14.1 times of those of traditional BT/CE and BTFp/CE composites, respectively; in fact, the BTF6(1200)/CE composite has the highest dielectric constant among non-semiconductive ceramic/polymer composites reported to date; meanwhile the dielectric loss of BTF6(1200)/CE is only about 0.276. The nature behind the excellent dielectric properties of BTF/CE composites was intensively discussed and proven to be attributed to the unique three-dimensional foam structure of BTF in CE resin. This study establishes a new method of preparing novel foam ceramics with three-dimensional interconnecting foam channels and a pure high-k ceramic skeleton as well as high-k ceramic/polymer composites with good processing characteristics at a very low loading of ceramics.
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JOURNAL OF CHEMICAL AND ENGINEERING DATA
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2013
·
IF 2.004
Xiaopo Wang,Kai Kang,Wei Wang,Yuansi Tian
Experimental density data of the binary mixtures of 3-(methylamino)propylamine with water, N-methyldiethanolamine, N,N-dimethylethanolamine and N,N-diethylethanolamine were reported at atmospheric pressure over the entire composition range at temperatures from (283.15 to 363.15) K. The densities were measured using an Anton Paar digital vibrating U-tube densimeter. Excess molar volumes of the mixture were calculated from the experimental densities and correlated as the Redlich–Kister equation. The optimized sets of parameters of the equation were obtained by the least-squares method at each temperature. Infinite dilution partial molar volumes and the corresponding excess partial molar volumes at infinite dilution were calculated and discussed. Thermal expansivities for the binary mixtures were presented.
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JOURNAL OF CHEMICAL AND ENGINEERING DATA
·
2013
·
IF 2.004
Zhicheng Xu,Shujuan Wang,Changhe Chen
Densities of and N2O solubilities in aqueous solutions of 1,4-butanediamine (BDA), 2-(diethylamino)-ethanol (DEEA), and their aqueous mixtures were measured at (298.15, 313.15, and 333.15) K, and viscosities were measured at (298.15, 303.15, 313.15, 323.15, and 333.15) K. The experiments cover the mole fraction ranges (1.95–14.3 mol %) BDA, (2.01–19.3 mol %) DEEA, and (3.63–16.7 mol %) BDA + (2.62–22.2 mol %) DEEA in the blended solutions. The results were compared with available data in the literature. The experimental density and viscosity data were correlated using two semi empirical correlations in the literature as functions of temperature and concentration of BDA and DEEA.
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FLUID PHASE EQUILIBRIA
·
2015
·
IF 2.2
Yang Yang,Qi Zhang,Yonghong Hu,Yonglan Li,Wenge Yang,Cuicui Cao,Limin Cheng
Data on corresponding solid–liquid equilibrium of mercaptosuccinic acid is essential for a preliminary study of industrial applications. In this paper, we focused on solubility and solution thermodynamics of mercaptosuccinic acid. By gravimetric method, the solid–liquid equilibrium of mercaptosuccinic acid was measured in (methanol + ethyl acetate) binary solvent mixtures from 278.15 K to 333.15 K under atmosphere pressure. The solubility data were then modeled using modified Apelblat equation, a variant of the combined nearly ideal binary solvent/Redich–Kister (CNIBS/R–K) model and Jouyban–Acree model. Computational results showed that the modified Apelblat equation and CNIBS/R–K model have the low MD (mean deviation). In addition, the thermodynamic properties of the solution process, including the Gibbs energy, enthalpy, and entropy were calculated by the van’t Hoff analysis.
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危险品化学品经营许可证（带存储）