Representation of Vapor-Liquid Equilibria Properties for Binary Mixtures Containing R1234ze(E) using Machine Learning Models
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Title
Representation of Vapor-Liquid Equilibria Properties for Binary Mixtures Containing R1234ze(E) using Machine Learning Models
Authors
Keywords
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Journal
JOURNAL OF PHASE EQUILIBRIA AND DIFFUSION
Volume 42, Issue 2, Pages 231-244
Publisher
Springer Science and Business Media LLC
Online
2021-03-18
DOI
10.1007/s11669-021-00874-0
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Note: Only part of the references are listed.- Experimental measurement and modelling of vapor-liquid equilibrium for 3,3,3- Trifluoropropene (R1243zf) and trans-1,3,3,3-Tetrafluoropropene (R1234ze(E)) binary system
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- Prediction of vapor–liquid equilibrium for binary mixtures containing R1234yf or R1234ze (E)
- (2018) Ali Barati-Harooni et al. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID
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- (2018) Xianyang Meng et al. JOURNAL OF CHEMICAL THERMODYNAMICS
- Isothermal Vapor–Liquid Equilibrium Measurements for the (R1234ze(E) + Ethane) System at Temperatures from 272.27 to 347.52 K
- (2018) Yue Liu et al. JOURNAL OF CHEMICAL AND ENGINEERING DATA
- Thermodynamic properties of hydrofluoroolefin (R1234yf and R1234ze(E)) refrigerant mixtures: Density, vapour-liquid equilibrium, and heat capacity data and modelling
- (2018) Saif ZS. Al Ghafri et al. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID
- Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
- (2017) Xiaozhen Hu et al. FLUID PHASE EQUILIBRIA
- Vapor liquid equilibrium measurements for difluoromethane (R32) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and fluoroethane (R161) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf)
- (2017) Xiaozhen Hu et al. FLUID PHASE EQUILIBRIA
- The Minkowski central partition as a pointer to a suitable distance exponent and consensus partitioning
- (2017) Renato Cordeiro de Amorim et al. PATTERN RECOGNITION
- A review of refrigerant R1234ze(E) recent investigations
- (2016) Adrián Mota-Babiloni et al. APPLIED THERMAL ENGINEERING
- Phase equilibrium for the binary mixture of {1,1-difluoroethane (R152a)+trans-1,3,3,3-tetrafluoropropene (R1234ze (E))} at various temperatures from 258.150 to 288.150K
- (2013) Zhi Yang et al. FLUID PHASE EQUILIBRIA
- Measurements of isothermal (vapour+liquid) equilibria data for {1,1,2,2-Tetrafluoroethane (R134)+trans-1,3,3,3-tetrafluoropropene (R1234ze(E))} at T=(258.150 to 288.150)K
- (2013) Xueqiang Dong et al. JOURNAL OF CHEMICAL THERMODYNAMICS
- Experimental measurement of vapor–liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E))+propane (R290))
- (2011) Xueqiang Dong et al. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID
- Vapor–Liquid Equilibria of the trans-1,3,3,3-Tetrafluoropropene (R1234ze(E)) + Isobutane (R600a) System at Various Temperatures from (258.150 to 288.150) K
- (2011) Xueqiang Dong et al. JOURNAL OF CHEMICAL AND ENGINEERING DATA
- (Vapour+liquid) equilibrium data for the binary system of {trifluoroiodomethane (R13I1)+trans-1, 3, 3, 3-tetrafluoropropene (R1234ze (E))} at various temperatures from (258.150 to 298.150)K
- (2011) Hao Guo et al. JOURNAL OF CHEMICAL THERMODYNAMICS
- Prediction of elastic modulus of normal and high strength concrete by support vector machine
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