Vapor-liquid equilibrium of 3, 3, 3-trifluoropropene with 1-ethyl-3-methyl-imidazolium tetrafluoroborate and 1-butyl-3-methyl-imidazolium tetrafluoroborate
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作者:
Jia, Xiucan
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn, Minist Educ, Xian 710049, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn, Minist Educ, Xian 710049, Peoples R China
Jia, Xiucan
[1
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Ma, Yutian
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn, Minist Educ, Xian 710049, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn, Minist Educ, Xian 710049, Peoples R China
Ma, Yutian
[1
]
Wang, Xiaopo
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn, Minist Educ, Xian 710049, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn, Minist Educ, Xian 710049, Peoples R China
Wang, Xiaopo
[1
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机构:
[1] Xi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn, Minist Educ, Xian 710049, Peoples R China
3, 3, 3-Trifluoropropene (R1243zf or HFO1243zf) is a promising refrigerant due to the low global warming potential and similar performance to R134a. Ionic liquids 1-ethyl-3-methyl-imidazolium tetrafluorobo-rate ([Emim][BF4]) and 1-butyl-3-methyl-imidazolium tetrafluoroborate ([Bmim][BF4]) are two potential absorbents with appropriate viscosity, good stability and absorption capacity to fluorine containing refrigerants. The phase behavior of refrigerant/ionic liquid mixtures is crucial for their deep applications. In this work, the vapor-liquid equilibrium of R1243zf with [Emim][BF4] and [Bmim][BF4] were measured based on the isochoric saturation method, and the non-random two liquid (NRTL) model was utilized to correlate the experimental results. The effects of different anions and cations on the liquidus molar frac-tion of R1243zf were studied. In addition, the Henry's constants and derived thermodynamic properties (enthalpy, entropy and Gibbs energy) for the two mixtures were calculated. Furthermore, the phase behavior of different HFO refrigerants (R1234ze(E), R1234yf and R1243zf) with [Emim][BF4] were com-pared and analyzed.(c) 2023 Elsevier B.V. All rights reserved.
机构:
China Univ Petr E China, Coll Chem & Chem Engn, Dongying 257061, Peoples R ChinaChina Univ Petr E China, Coll Chem & Chem Engn, Dongying 257061, Peoples R China
Lue Renqing
Cao Zuogang
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China Univ Petr E China, Coll Chem & Chem Engn, Dongying 257061, Peoples R ChinaChina Univ Petr E China, Coll Chem & Chem Engn, Dongying 257061, Peoples R China
Cao Zuogang
Shen Guoping
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China Univ Petr E China, Coll Chem & Chem Engn, Dongying 257061, Peoples R ChinaChina Univ Petr E China, Coll Chem & Chem Engn, Dongying 257061, Peoples R China
机构:
Korea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South KoreaKorea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South Korea
Choi, Myungho
Lim, Jungae
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Korea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South KoreaKorea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South Korea
Lim, Jungae
Kwon, Sunil
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Korea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South KoreaKorea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South Korea
Kwon, Sunil
Jeong, Kwanyong
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Korea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South KoreaKorea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South Korea
Jeong, Kwanyong
Park, Ji Hoon
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Korea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South KoreaKorea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South Korea
Park, Ji Hoon
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Byun, Jaewon
Kim, Soo Min
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Korea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South KoreaKorea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South Korea
Kim, Soo Min
Han, Jee-hoon
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Pohang Univ Sci & Technol, Dept Chem Engn, Pohang 37673, South KoreaKorea Res Inst Chem Technol, CO2 & Energy Res Ctr, Daejeon 34114, South Korea