The experimental investigation of the vapour liquid phase equilibrium for (ammonia+2,3,3,3-tetrafluoroprop-1-ene) system

被引：14

作者：

Zhao, Yanxing ^{[1
,2
]}

Dong, Xueqiang ^{[1
]}

Zhong, Quan ^{[1
,2
]}

Li, Huiya ^{[1
]}

Zhang, Haiyang ^{[3
]}

Gong, Maoqiong ^{[1
]}

Shen, Jun ^{[1
]}

机构：

[1] Chinese Acad Sci, Tech Inst Phys & Chem, Key Lab Cryogen, POB 2711, Beijing 100190, Peoples R China

[2] Univ Chinese Acad Sci, Beijing 100039, Peoples R China

[3] Chinese Acad Sci, Tech Inst Phys & Chem, POB 2711, Beijing 100190, Peoples R China

来源：

JOURNAL OF CHEMICAL THERMODYNAMICS | 2017年 / 113卷

关键词：

(Vapour plus liquid) equilibrium Ammonia; 2,3,3,3-Tetrafluoroprop-1-ene; Azeotropic refrigerant; EQUATION-OF-STATE; AMMONIA; R1234YF; REFRIGERATION; PRESSURE;

D O I：

10.1016/j.jct.2017.06.018

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Searching for mixed alternative refrigerants with less influence on global warming is one of the main tasks of the refrigeration industry. This paper presents the vapour liquid phase equilibrium and vapour liquid liquid phase equilibrium data of (ammonia + 3,3,3-tetrafluoroprop-1-ene) system at temperature from 243.150 K to 283.150 K. The vapour pressures of 3,3,3-tetrafluoroprop-1-ene were compared with Refprop 9.1, and the maximum deviation of pressure is 0.0007 MPa. The VLE and VLLE data were regressed by the PR-MHV2-NRTL model. Good reproduction was shown with the maximum RT = 0.009 K, Rp = 0.0040 MPa, Rx = 0.013 and Ry = 0.013. The homogeneous or heterogeneous azeotropic behaviours were found for the systems concerned over the temperature ranges investigated. The present results suggest that the volumetric refrigeration capacity of (ammonia + 2,3,3,3-tetrafluoroprop-1-ene) azeotropic mixture is 15% higher than that of ammonia and 79% higher than that of 2,3,3,3-tetrafluoroprop-1-ene. (C) 2017 Elsevier Ltd.

引用

页码：257 / 262

页数：6

共 49 条

[31] Vapor-liquid and vapor-liquid-liquid equilibrium measurements and correlation of the binary mixtures 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) + (tetrafluoromethane (R14), trifluoromethane (R23), octafluoropropane (R218), nitrogen (R728) and argon (R740)) and ethane (R170) + trifluoromethane (R23) [J].

Kochenburger, T. M. ;

Gomse, D. ;

Tratschitt, I. ;

Zimmermann, A. ;

Grohmann, S. .

FLUID PHASE EQUILIBRIA, 2017, 450 :13-23

[32] Isothermal (vapour-liquid) equilibrium for the binary {3,3,3-trifluoropropene (R1243zf) + propane(R290)} system at temperatures from 243.150 K to 288.150 K [J].

Ding, Li ;

Yao, Xiaoyu ;

Hou, Yu ;

Zhao, Yanxing ;

Dong, Xueqiang ;

Gong, Maoqiong .

JOURNAL OF CHEMICAL THERMODYNAMICS, 2020, 144

[33] Experimental vapour-liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane [J].

Subramoney, Shalendra Clinton ;

Valtz, Alain ;

Coquelet, Christophe ;

Richon, Dominique ;

Naidoo, Paramespri ;

Ramjugernath, Deresh .

JOURNAL OF CHEMICAL THERMODYNAMICS, 2013, 61 :18-26

[34] Isothermal Vapor-Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene+1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K [J].

Conradie, Francois J. ;

Crouse, Philippus L. ;

Courtial, Xavier ;

Nelson, Wayne M. ;

van der Walt, Isaak J. ;

Ramjugernath, Deresh .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2014, 59 (01) :82-88

[35] Isothermal Vapor-Liquid Equilibrium for the Binary System of Trans-1,3,3,3-tetrafluoropropene and 1,1,1,3,3-Pentafluoropropane [J].

Tang, Nian ;

Gu, Wenguo ;

Sun, Dongwei ;

Tang, Xiaobo ;

Yang, Zhiqiang ;

Lu, Jian .

INTERNATIONAL JOURNAL OF THERMOPHYSICS, 2023, 44 (08)

[36] Isothermal Vapor-Liquid Equilibrium Data for the 1,1,2,3,3,3-Hexafluoroprop-1-ene+1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (292 to 352) K and Pressures up to 2.6 MPa [J].

Conradie, Francois J. ;

Crouse, Philippus L. ;

Courtial, Xavier ;

Nelson, Wayne M. ;

van der Walt, Isaak J. ;

Ramjugernath, Deresh .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2015, 60 (03) :966-969

[37] Subcooled liquid density measurements and PvT measurements in the vapor phase for 3,3,3-trifluoroprop-1-ene (R1243zf) [J].

Di Nicola, Giovanni ;

Brown, J. Steven ;

Fedele, Laura ;

Securo, Matteo ;

Bobbo, Sergio ;

Zilio, Claudio .

INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2013, 36 (08) :2209-2215

[38] Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane) [J].

Williams-Wynn, Mark D. ;

Naidoo, Paramespri ;

Ramjugernath, Deresh .

JOURNAL OF CHEMICAL THERMODYNAMICS, 2018, 121 :79-90

[39] Experimental investigation and thermodynamic modeling of equilibrium extraction of gold(III) from hydrochloric acid in 1-butyl-3-methylimidazolium hexafluorophosphate [J].

Farzam, Samira ;

Feyzi, Farzaneh .

FLUID PHASE EQUILIBRIA, 2021, 527

[40] Vapor Liquid Phase Equilibrium for Azeotropic Isobutane plus trans-1,3,3,3-Tetrafluoropropene plus Trifluoroiodomethane System at Temperatures from 243.150 to 283.150 K [J].

Zhao, Yanxing ;

Zhong, Quan ;

Wang, Jingzhou ;

Dong, Xueqiang ;

Li, Huiya ;

Gao, Bo ;

Shen, Jun ;

Gong, Maoqiong .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2018, 63 (03) :812-821

← 1 2 3 4 5 →