Vapor-liquid equilibria for the 1,1,1-tirfluoroethane + isobutene system

机译：1,1,1-Tirforoorhane +异丁烯体系的蒸汽液平衡

获取原文

页面导航

摘要
著录项
相似文献
相关主题

摘要

Binary vapor liquid equilibrium data were measured for the 1,1,1-tirfluoroethane (HFC-143a) + isobutene system at temperature from 273.15 K to 318.15 K. These experiments were carried out with a circulating-type apparatus with on-line gas chromatography. The experimental data were correlated well by Peng-Robinson equation of state using the Wong-Sandler mixing rules.

机译：在273.15k至318.15k的温度下测量二元蒸汽液体平衡数据（HFC-143A）+异丁烯系统。通过带在线气相色谱法的循环式设备进行这些实验。使用Wong-Sandler混合规则，彭罗宾逊方程的实验数据很好地相关。

著录项

来源
《International Conference on Separation Science and Technology》|2007年||共4页
会议地点
作者
Yong Ju Yun; Jihoon Im; Hyo Won Kim; Hwayong Kim;
展开▼
作者单位

展开▼
会议组织
原文格式 PDF
正文语种
中图分类分离过程;
关键词
Phase Equilibria; 1; isobutene; Circulating type apparatus; Equation of state; 1; 1-trifluoroethane (HFC-143a);

机译：相平衡;1;异丁烯;循环式装置;状态方程;1;1-三氟乙烷（HFC-143A）;

相似文献

外文文献
中文文献
专利

1. (Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system [J] . Yongju Yun, Jihoon Im, Hwayong Kim The Journal of Chemical Thermodynamics . 2008,第5期

机译：{1,1,1-三氟乙烷（HFC-143a）+异丁烯}系统的（蒸气+液体）平衡
2. Vapor-liquid equilibria for the 1,1,1,2-tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems [J] . Peng Hu, Long-Xiang Chen, Ze-Shao Chen Fluid Phase Equilibria . 2013,第Null期

机译：1,1,1,2-四氟乙烷（HFC-134a）+ 1,1,1,2,3,3,3,3-七氟丙烷（HFC-227ea）和1,1,1-三氟乙烷（ HFC-143a）+ 2,3,3,3-四氟丙-1-烯（HFO-1234yf）系统
3. Vapor-liquid equilibria of the carbon dioxide (CO2)+2,2-dichloro-1,1,1-trifluoroethane (R123) system and carbon dioxide (CO2)+1-chloro-1,2,2,2-tetrafluoroethane (R124) system [J] . Jeong K, Im J, Lee G, Fluid Phase Equilibria . 2007,第1期

机译：二氧化碳（CO2）+ 2,2-二氯-1,1,1-三氟乙烷（R123）系统和二氧化碳（CO2）+ 1-氯-1,2,2,2-四氟乙烷（ R124）系统
4. Vapor-liquid equilibria for the 1,1,1-tirfluoroethane + isobutene system [C] . Yong Ju Yun, Jihoon Im, Hyo Won Kim, International Conference on Separation Science and Technology(ICSST'2007); 20071014-16; Beijing(CN) . 2007

机译：1,1,1-三氟乙烷+异丁烯体系的汽液平衡
5. Vapor-liquid equilibria of n-heptane/n-propanol/1, chlorobutane system and a theoroetical study of gas-solid equilibria. [D] . Ashraf, Feroz Ali. 1979

机译：正庚烷/正丙醇/ 1的气液平衡，氯丁烷体系和气固平衡的理论研究。
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. MEASUREMENTS AND THERMODYNAMIC MODELING OF VAPOR-LIQUID EQUILIBRIA FOR BINARY SYSTEMS OF ISOPROPYL CHLOROACETATE WITH CYCLOHEXANE, ISOPROPANOL AND BENZENE AT 101.3 kPa [O] . Dongmei Xu, Rui Li, Lianzheng Zhang, 2019

机译：环己烷，异丙醇和101.3kPa氯乙酸异丙酯二元系统蒸汽液体平衡的测量和热力学建模
8. Vapor-liquid equilibria for copolymer+solvent systems: Effect of intramolecular repulsion [R] . Gupta, R. B. , Prausnitz, J. M. 1995

机译：共聚物+溶剂体系的汽液平衡：分子内排斥的影响

Vapor-liquid equilibria for the 1,1,1-tirfluoroethane + isobutene system

摘要

著录项

相似文献

相关主题

期刊订阅