Bubble point pressures of binary mixtures of ethanol with propane, dimethyl ether or trans-1,3,3,3-tetrafluoropropene and correlation with equations of state and Wong-Sandler mixing rules

被引：7
作者：
Nakazawa, Misaki [1 ]
Tsuji, Tomoya [2 ,3 ]
Lai, Andrea Jia Xin [2 ]
Zaini, Nabilah Binti [2 ]
Hoshina, Taka-aki [1 ]
Otake, Katsuto [4 ]
Yoshida, Atsumasa [3 ]
机构：
[1] Nihon Univ, Coll Ind Technol, Narashino, Chiba, Japan
[2] Univ Teknol Malaysia, Malaysia Japan Int Inst Technol, Kuala Lumpur, Malaysia
[3] Osaka Prefecture Univ, Dept Mech Engn, Sakai, Osaka, Japan
[4] Tokyo Univ Sci, Faulty Engn, Shinjyuku Ku, Tokyo, Japan
来源：
FLUID PHASE EQUILIBRIA | 2020年 / 522卷
关键词：
Bubble point pressure; Propane; Dimethyl ether; trans-1,3,3,3-Tetrafluoropropene (R1234ze(E)); Ethanol; VAPOR-LIQUID-EQUILIBRIUM; PLUS ETHANOL; THERMODYNAMIC PROPERTIES; R1234ZE(E); R1234YF; DENSITY; SYSTEM;
D O I：
10.1016/j.fluid.2020.112764
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
For the design of spray propellants, bubble point pressures were measured for binary mixtures of ethanol with propane, dimethyl ether (DME) or trans-1,3,3,3-tetrafluoropropene (R1234ze(E)), with a static type apparatus at (293.15-313.15) K. Experimental data were correlated with the Peng-Robinson (PR) and Stryjek-Vera (PRSV) equations of state using the Wong-Sandler (WS) mixing rules. The NRTL activity coefficient model in the WS mixing rules was effective for correlation of systems that exhibited large non-idealities (ethanol - propane, ethanol - R1234ze(E)). Correlation of the bubble point pressures with the PRSV equation of state and WS mixing rules was to within an average of 2.391% absolute deviation in pressure for all systems, which is considered to be sufficient for design of spray devices with propellants that have low global warming potential. (C) 2020 Elsevier B.V. All rights reserved.
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页数：7
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