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Vapor-liquid phase equilibrium and modeling for binary and ternary mixtures at high pressure

机译：高压下汽液相平衡和二元和三元混合物的建模

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Bezanehtak Keivan Chemical Engineering Faculty of Engineering UNSW;
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年度 2002
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1. Measurements and Correlation of Isobaric Vapor-Liquid Equilibrium Data for Binary Mixtures of Furan, Oxolane, and Furan-2-Carbaldehyde and Application of the Binary Model Parameters for Further Prediction of the Ternary System [J] . Chen Qianyun, Zhang Lidong, Zhang Hui, Journal of Chemical and Engineering Data: the ACS Journal for Data . 2020,第5期

机译：呋喃，奥克洛甲酸盐和呋喃 - 2-甲醛二元混合物的异蒸气液平衡数据的测量和相关性及二元模型参数的应用，以进行三元系统的进一步预测
2. Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 6. Total pressure data and G(E) for binary and ternary mixtures containing 1, 1-dimethlethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K [J] . Alonso C., Montero EA., Chamorro CR., Fluid Phase Equilibria . 2004,第2期

机译：汽油中辛烷增强添加剂的蒸气液平衡 - 6.含有1,1-二甲乙基甲基醚（MTBE），甲醇和正己烷的二元和三元混合物的总压力数据和G（e），313.15k
3. Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 5. Total pressure data and GE for binary and ternary mixtures containing 1,1-dimethylpropyl methyl ether (TAME), 1-propanol and n-hexane at 313.15 K [J] . Alonso C., Montero EA., Chamorro UR., Fluid Phase Equilibria . 2003,第1a2期

机译：汽油中辛烷值提高添加剂的汽液平衡-5.在313.15 K下，含有1,1-二甲基丙基甲基醚（TAME），1-丙醇和正己烷的二元和三元混合物的总压力数据和GE
4. Phase equilibrium model and partial molar volume calculation for dimethylformamide and CO2 binary mixture at high pressure [C] . Liu Kecun, Zheng Lan, Wang Yuqi, 2011 International Conference on Materials for Renewable Energy Environment . 2011

机译：高压下二甲基甲酰胺和CO 2 二元混合物的相平衡模型和部分摩尔体积计算
5. Multiphase equilibrium behavior of ethane, nitrous oxide and carbon dioxide + N-alkanol binary and ternary mixtures [D] . Lam, Daniel Haw 1990

机译：乙烷，一氧化二氮和二氧化碳+ N-烷醇二元和三元混合物的多相平衡行为
6. Molecular simulation data for the vapor-liquid phase equilibria of binary mixtures of HFO-1123 with R-32 R-1234yf R-1234ze(E) R-134a and CO2 and their modelling by the PCP-SAFT equation of state [O] . Gabriele Raabe 2019

机译：HFO-1123与R-32R-1234yfR-1234ze（E）R-134a和CO2的二元混合物的汽液相平衡的分子模拟数据及其通过状态PCP-SAFT方程进行建模
7. Computation of Isobaric Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures of Methanol, Water, and Ethanoic Acid from T, p, x, and HmE Measurements [O] . Daming Gao, Hui Zhang, Peter Lücking, 2012

机译：来自T，P，X和HME测量的二元和甲醇，水和乙酸的二元混合物的异氧化物蒸气液平衡数据计算
8. Vapor-Liquid Equilibrium of Binary Mixtures in the Extended Critical Region. I. Thermodynamic Model [R] . Rainwater, J. C. 1989

机译：扩展临界区域二元混合物的汽液平衡。 I.热力学模型

Vapor-liquid phase equilibrium and modeling for binary and ternary mixtures at high pressure

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