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VAPOR–LIQUID–LIQUID EQUILIBRIUM MEASUREMENTS AND MODELING OF METHANETHIOL OR ETHANETHIOL OR OR 1-BUTANETHIOL IN METHANE + WATER TERNARY SYSTEMS AT 303, 335, AND 365 K AND PRESSURE UP TO 9 MPA

机译：在303、335和365 K的甲烷和水三元体系中，蒸气-液体-液体的平衡测量和甲醇，乙醇，或1-丁醇的甲醇和水的建模

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International audience

机译：国际观众

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Awan Javeed; Coquelet Christophe; Tsivintzelis Ioannis; Kontogeorgis Georgios M.;
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年度 2015
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1. 丙烯-甲醇-水三元体系汽液相平衡研究(英) [J] . 陈晓晖, 王春艳, 许锡恩, 天津大学学报：英文版 . 1999,第001期
2. Ternary Vapor - Liquid Equilibrium Measurements and Modeling of Ethylene Glycol (1) + Water (2) + Methane (3) Systems at 6 and 12.5 MPa [J] . Kruger Francois J., Danielsen Marie V., Kontogeorgis Georgios M., Journal of Chemical and Engineering Data: the ACS Journal for Data . 2018,第5期

机译：三元蒸汽 - 液体平衡测量和乙二醇（1）+水（2）+甲烷（3）系统在6和12.5MPa的情况下建模
3. Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213-299 K and pressures up to 16 MPa [J] . Lovseth Sigurd Weidemann, Austegard Anders, Westman Snorre Foss, Fluid Phase Equilibria . 2018,第期

机译：二氧化碳加（CO2 + Ar）系统的热力学：改进的参考混合物模型和蒸汽 - 固体，液体固体和蒸气 - 液固 - 固相平衡数据213-299 K和压力高达16 MPa
4. Phase Equilibrium Measurements and Modeling of 1-Propanethiol+1-Butanethiol + CH4 in Methane Ternary System at 303, 336, and 368 K and Pressure Up to 9 MPa [J] . Awan Javeed A., Coquelet Christophe, Tsivintzelis Ioannis, Journal of Chemical and Engineering Data: the ACS Journal for Data . 2016,第1期

机译：303、336和368 K且压力高达9 MPa的甲烷三元体系中1-丙硫醇+ 1-丁硫醇+ CH4的相平衡测量和建模
5. MEASUREMENTS AND MODELING OF VAPOR-LIQUID EQUILIBRIA IN BINARY SYSTEMS OF METHANE + {N-C_5, NC_6, OR BTEX COMPOUNDS) AT CRYOGENIC TEMPERATURES AND HIGH PRESSURES [C] . Eric F. May, Sean McCallum, Mohamed E. Kandil, . 2011

机译：低温和高压下甲烷+ {N-C_5，NC_6或BTEX化合物）的二元体系中气液平衡的测量和建模
6. Vapor-liquid equilibrium in the systems argon-oxygen and ammonia-water: Measurements and modeling for industrial and planetary applications. [D] . Parikh, Nimmi Chandra. 1997

机译：氩氧和氨水系统中的气液平衡：工业和行星应用的测量和建模。
7. Extremely Low Vapor‐Pressure Data as Access to PC‐SAFT Parameter Estimation for Ionic Liquids and Modeling of Precursor Solubility in Ionic Liquids [O] . Mark Bülow, Moritz Greive, Dr. Dzmitry H. Zaitsau, 2021

机译：极低的蒸气压数据作为离子液体的PC-SAFT参数估计和离子液体中前体溶解度的建模
8. Vapor–Liquid–Liquid Equilibrium Measurements and Modeling of Ethanethiol + Methane + Water, 1-Propanethiol + Methane + Water and 1-Butanethiol + Methane + Water Ternary Systems at 303, 335, and 365 K and Pressure Up to 9 MPa [O] . Awan Javeed, Kontogeorgis Georgios, Tsivintzelis Ioannis, 2013

机译：乙烷硫醇+甲烷+水，1-丙硫醇+甲烷+水和1-丁硫醇+甲烷+水三元体系的汽液液体平衡测量和模拟，303,335和365 K，压力高达9 mpa
9. High-Pressure Vapor-Liquid Equilibria in Ternary Systems Containing Two Miscible Liquids and One Supercritical Gas [R] . Topliss, R. J., Dimitrelis, D., Prausnitz, J. M. 1982

机译：含有两种可混溶液体和一种超临界气体的三元体系中的高压汽液平衡

VAPOR–LIQUID–LIQUID EQUILIBRIUM MEASUREMENTS AND MODELING OF METHANETHIOL OR ETHANETHIOL OR OR 1-BUTANETHIOL IN METHANE + WATER TERNARY SYSTEMS AT 303, 335, AND 365 K AND PRESSURE UP TO 9 MPA

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