Measurement of critical parameters for the binary mixture of R744 (carbon dioxide)+R1234yf (2,3,3,3-tetrafluoropro-1-ene)

被引:11
作者
Yao, Xiaoyu [1 ]
Shen, Jun [1 ]
Kang, HuiFang [1 ]
Li, Zhenxing [1 ,2 ]
Dong, Xueqiang [2 ,3 ]
Gong, Maoqiong [2 ,3 ]
机构
[1] Beijing Inst Technol, Sch Mech Engn, Beijing 100081, Peoples R China
[2] Chinese Acad Sci, Tech Inst Phys & Chem, Key Lab Cryogen, POB 2711, Beijing 100190, Peoples R China
[3] Univ Chinese Acad Sci, Beijing 100039, Peoples R China
基金
中国国家自然科学基金;
关键词
Variable -volume method; Critical parameters; Metal -bellows volumeter; Critical density; Carbon dioxide; 3-Tetrafluoropro-1-ene; LOW-GRADE HEAT; TRANSCRITICAL POWER CYCLES; CARBON-DIOXIDE BLENDS; RANKINE CYCLES; THERMODYNAMIC ANALYSIS; WORKING FLUIDS; CO2; TEMPERATURES; PERFORMANCE; PRESSURES;
D O I
10.1016/j.jct.2022.106978
中图分类号
O414.1 [热力学];
学科分类号
摘要
The critical parameters including critical temperature, critical pressure, critical densities, and mole fraction for the binary mixture of R744 (carbon dioxide) + R1234yf (2,3,3,3-tetrafluoropro-1-ene) mixture were measured using a metal-bellows variable volumeter. The critical point was determined by visually observing the critical opalescence and reappearance of the meniscus. The expanded combined uncertainties of the critical temperature, critical pressure, critical density, and composition measurements were assessed to be less than 50 mK, 21 kPa, 0.006, and 0.015 (k = 2, 0.95 level of confidence), respectively. The experimental critical properties for the mixture correlated by Redlich-Kister equations were 0.15 % for critical temperature, 0.46 % for critical pressure, 0.10 % for critical density, and 0.08 % for critical molar volume. The mixture formed by mixing about 0.15 M fraction of R1234yf can increase the critical temperature by about 20 K and reduce the critical pressure by about 0.4 MPa compared with the pure material of CO2.
引用
收藏
页数:6
相关论文
共 31 条
[11]  
Lemmon E. W., 2018, NIST standard reference database 23: reference fluid thermodynamic and transport properties-REFPROP, version 10.0, NIST, standard reference data program, DOI DOI 10.18434/T4D303
[12]   Critical temperatures and pressures of several binary and ternary mixtures concerning the alkylation of 2-methylpropane with 1-butene in the presence of methane or carbon dioxide [J].
Li, Junfen ;
Qin, Zhangfeng ;
Wang, Guofu ;
Dong, Mei ;
Wang, Jianguo .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2007, 52 (05) :1736-1740
[13]   Thermodynamic analysis and comparison between CO2 transcritical power cycles and R245fa organic Rankine cycles for low grade heat to power energy conversion [J].
Li, L. ;
Ge, Y. T. ;
Luo, X. ;
Tassou, S. A. .
APPLIED THERMAL ENGINEERING, 2016, 106 :1290-1299
[14]   GAS-LIQUID CRITICAL PROPERTIES OF METHYLAMINE + NITROUS-OXIDE AND METHYLAMINE + ETHYLENE BINARY-MIXTURES [J].
LI, LX ;
KIRAN, E .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1988, 33 (03) :342-344
[15]   Vapor-liquid equilibrium measurements for binary mixtures of carbon dioxide (CO2)+2,3,3,3-Tetrafluoroprop-1-ene (R-1234yf) and carbon dioxide (CO2)+3,3,3-Trifluoropropene (R-1243zf) [J].
Li, Shuhao ;
Peng, Shuzhou ;
Yang, Zhen ;
Duan, Yuanyuan .
FLUID PHASE EQUILIBRIA, 2022, 561
[16]  
More J. J., 1978, Proceedings of the Biennial Conference on numerical analysis, P105
[17]   HFO refrigerants: A review of present status and future prospects [J].
Nair, Vipin .
INTERNATIONAL JOURNAL OF REFRIGERATION, 2021, 122 :156-170
[18]   Prediction of true critical temperature of multi-component mixtures:Extending fast estimation methods [J].
Najafi, Hamidreza ;
Maghbooli, Babak ;
Sobati, Mohammad Amin .
FLUID PHASE EQUILIBRIA, 2015, 392 :104-126
[19]   Supplementary measurements of the (p,p,T) relation of carbon dioxide in the homogeneous region at T=313 K and on the coexistence curve at T=304 K [J].
Nowak, P ;
Tielkes, T ;
Kleinrahm, R ;
Wagner, W .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1997, 29 (08) :885-889
[20]   Optimization of the self-condensing CO2 transcritical power cycle using solar thermal energy [J].
Pan, Lisheng ;
Li, Bing ;
Shi, Weixiu ;
Wei, Xiaolin .
APPLIED ENERGY, 2019, 253