Chemical Properties of Norflurane (CAS 811-97-2)

InChI

InChI=1S/C2H2F4/c3-1-2(4,5)6/h1H2

InChI Key

LVGUZGTVOIAKKC-UHFFFAOYSA-N

Formula

C2H2F4

SMILES

FCC(F)(F)F

Molecular Weight¹

102.03

CAS

811-97-2

Other Names

• 1,1,1,2-Tetrafluoroethane
• 1,2,2,2-Tetrafluoroethane
• CF3CH2F
• Ethane, 1,1,1,2-tetrafluoro-
• Freon 134a
• HFA-134a
• NORFLURAN
• R 134a
• R-134a
• REFRIGERANT-134A

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• ρ_m,g : Gas Amount Density (mol/m³).
• I_np : Non-polar retention indices.
• D^*_i : Self diffusion coefficient (m²/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.2774		Relay (1.0) Calculated Property
ΔfG°	-810.44	kJ/mol	Joback Calculated Property
ΔfH°gas	-891.85	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	5.84	kJ/mol	Joback Calculated Property
ΔvapH°	18.83	kJ/mol	Relay (1.0) Calculated Property
IE	12.92	eV	Relay (1.0) Calculated Property
log10WS	-0.76		Relay (1.0) Calculated Property
logPoct/wat	1.518		Crippen Calculated Property
McVol	46.120	ml/mol	McGowan Calculated Property
Pc	[4029.00; 4068.00]	kPa
Pc	4065.00	kPa	KDB
Pc	4051.00	kPa	Critical Parameters and Vapor Pressures Measurements of Hydrofluoroethers at High Temperatures
Pc	4053.00	kPa	Critical Parameters Measurements of Four HFE + HFC Binary Systems: Pentafluoromethoxyethane (HFE-245Mc) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
Pc	4053.00	kPa	Critical Properties of Four HFE + HFC Binary Systems: Trifluoromethoxymethane (HFE-143m) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
Pc	4048.10 ± 5.00	kPa	NIST
Pc	4048.20 ± 3.00	kPa	NIST
Pc	4047.80 ± 5.00	kPa	NIST
Pc	4054.00 ± 8.00	kPa	NIST
Pc	4052.00 ± 9.00	kPa	NIST
Pc	4055.10 ± 2.00	kPa	NIST
Pc	4068.00 ± 10.00	kPa	NIST
Pc	4055.00 ± 6.00	kPa	NIST
Pc	Outlier 4029.00 ± 6.00	kPa	NIST
Pc	4064.00 ± 10.00	kPa	NIST
Pc	4067.00 ± 2.70	kPa	NIST
Pc	4065.00 ± 8.00	kPa	NIST
Pc	4067.00 ± 10.00	kPa	NIST
ρc	[507.09; 515.15]	kg/m3
ρc	507.09 ± 5.10	kg/m3	NIST
ρc	509.13 ± 3.06	kg/m3	NIST
ρc	511.17 ± 5.10	kg/m3	NIST
ρc	509.13 ± 2.04	kg/m3	NIST
ρc	508.11 ± 5.10	kg/m3	NIST
ρc	511.17 ± 3.06	kg/m3	NIST
ρc	Outlier 515.15 ± 2.55	kg/m3	NIST
ρc	507.09 ± 5.10	kg/m3	NIST
ρc	512.20 ± 5.10	kg/m3	NIST
ρc	508.11 ± 3.06	kg/m3	NIST
ρc	512.20 ± 2.04	kg/m3	NIST
Inp	[219.00; 219.00]
Inp	219.00		NIST
Inp	219.00		NIST
Inp	219.00		NIST
Tboil	[246.60; 247.10]	K
Tboil	246.60	K	KDB
Tboil	246.60	K	NIST
Tboil	247.10 ± 2.00	K	NIST
Tc	[373.05; 374.30]	K
Tc	374.30	K	KDB
Tc	374.07 ± 0.04	K	NIST
Tc	374.07 ± 0.02	K	NIST
Tc	374.07 ± 0.02	K	NIST
Tc	374.08 ± 0.02	K	NIST
Tc	373.80 ± 0.50	K	NIST
Tc	374.11 ± 0.05	K	NIST
Tc	374.11 ± 0.03	K	NIST
Tc	374.25 ± 0.05	K	NIST
Tc	374.18 ± 0.10	K	NIST
Tc	374.20 ± 0.10	K	NIST
Tc	Outlier 373.05 ± 0.30	K	NIST
Tc	374.25 ± 0.15	K	NIST
Tc	374.30 ± 0.01	K	NIST
Tc	374.27 ± 0.10	K	NIST
Tfus	172.00	K	KDB
Ttriple	[169.85; 169.85]	K
Ttriple	169.85 ± 0.01	K	NIST
Ttriple	169.85 ± 0.01	K	NIST
Ttriple	169.85 ± 0.02	K	NIST
Vc	0.198	m3/kmol	KDB
Zc	0.2586240		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[71.67; 97.89]	J/mol×K	[239.01; 369.61]
Cp,gas	71.67	J/mol×K	239.01	Joback Calculated Property
Cp,gas	76.59	J/mol×K	260.78	Joback Calculated Property
Cp,gas	81.27	J/mol×K	282.54	Joback Calculated Property
Cp,gas	85.74	J/mol×K	304.31	Joback Calculated Property
Cp,gas	89.99	J/mol×K	326.08	Joback Calculated Property
Cp,gas	94.04	J/mol×K	347.85	Joback Calculated Property
Cp,gas	97.89	J/mol×K	369.61	Joback Calculated Property
ΔfusH	2.01	kJ/mol	169.40	NIST
ΔvapH	[22.00; 26.40]	kJ/mol	[180.00; 321.00]
ΔvapH	26.40	kJ/mol	180.00	NIST
ΔvapH	25.00	kJ/mol	200.00	NIST
ΔvapH	23.80	kJ/mol	220.00	NIST
ΔvapH	23.70	kJ/mol	233.50	NIST
ΔvapH	22.70	kJ/mol	240.00	NIST
ΔvapH	22.00	kJ/mol	321.00	NIST
ν	[7.9000000e-08; 0.0000002]	m2/s	[302.99; 368.26]
ν	0.0000002	m2/s	302.99	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
ν	0.0000001	m2/s	312.86	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
ν	0.0000001	m2/s	322.92	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
ν	0.0000001	m2/s	332.92	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
ν	0.0000001	m2/s	342.90	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
ν	9.7900000e-08	m2/s	352.89	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
ν	8.5600000e-08	m2/s	363.27	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
ν	7.9000000e-08	m2/s	368.26	Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
Pvap	[84.10; 3245.53]	kPa	[243.10; 363.18]
Pvap	84.23	kPa	243.10	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
Pvap	84.10	kPa	243.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	84.50	kPa	243.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	92.40	kPa	245.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	101.40	kPa	247.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	106.12	kPa	248.08	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
Pvap	106.40	kPa	248.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	111.10	kPa	249.15	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	121.40	kPa	251.16	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	127.20	kPa	252.12	PVTx properties in the gas phase for binary R290/R134a system
Pvap	133.58	kPa	253.13	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	133.60	kPa	253.13	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	132.70	kPa	253.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	133.50	kPa	253.15	Isothermal vapour + liquid equilibrium measurements and correlation for the pentafluoroethane + cyclopropane and the cyclopropane + 1,1,1,2-tetrafluoroethane binary systems
Pvap	132.50	kPa	253.15	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	131.00	kPa	253.15	Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
Pvap	144.30	kPa	255.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	151.40	kPa	256.18	PVTx properties in the gas phase for binary R290/R134a system
Pvap	157.10	kPa	257.16	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	163.90	kPa	258.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	163.90	kPa	258.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	162.00	kPa	258.20	Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap	162.00	kPa	258.20	Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
Pvap	170.60	kPa	259.17	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	178.50	kPa	260.19	PVTx properties in the gas phase for binary R290/R134a system
Pvap	185.00	kPa	261.16	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	193.00	kPa	262.20	Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap	193.00	kPa	262.20	Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
Pvap	200.47	kPa	262.99	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	200.48	kPa	263.00	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	199.39	kPa	263.01	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
Pvap	200.20	kPa	263.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	200.60	kPa	263.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	200.60	kPa	263.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	202.60	kPa	263.15	Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
Pvap	203.00	kPa	263.15	Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
Pvap	195.70	kPa	263.43	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	209.60	kPa	264.20	PVTx properties in the gas phase for binary R290/R134a system
Pvap	216.40	kPa	265.13	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	233.70	kPa	267.13	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	243.30	kPa	268.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	245.50	kPa	268.15	Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
Pvap	243.30	kPa	268.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	244.30	kPa	268.21	PVTx properties in the gas phase for binary R290/R134a system
Pvap	252.10	kPa	269.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	271.60	kPa	271.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	283.00	kPa	272.14	PVTx properties in the gas phase for binary R290/R134a system
Pvap	286.00	kPa	272.20	Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
Pvap	286.00	kPa	272.20	Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap	292.10	kPa	273.13	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	292.70	kPa	273.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	294.20	kPa	273.15	Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Pvap	294.12	kPa	273.15	Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
Pvap	292.80	kPa	273.15	Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
Pvap	291.80	kPa	273.15	Isothermal vapour + liquid equilibrium measurements and correlation for the pentafluoroethane + cyclopropane and the cyclopropane + 1,1,1,2-tetrafluoroethane binary systems
Pvap	294.30	kPa	273.17	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	295.50	kPa	273.31	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	295.50	kPa	273.31	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	287.10	kPa	273.32	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	313.90	kPa	275.13	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	314.60	kPa	275.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	326.10	kPa	276.09	PVTx properties in the gas phase for binary R290/R134a system
Pvap	337.20	kPa	277.16	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	339.50	kPa	277.22	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	353.00	kPa	278.15	Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
Pvap	349.60	kPa	278.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	351.20	kPa	278.17	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	361.50	kPa	279.16	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	364.00	kPa	279.24	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	374.90	kPa	280.13	PVTx properties in the gas phase for binary R290/R134a system
Pvap	387.30	kPa	281.16	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	389.70	kPa	281.25	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	404.00	kPa	282.55	Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
Pvap	411.00	kPa	282.60	Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
Pvap	411.00	kPa	282.60	Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap	412.95	kPa	283.03	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
Pvap	414.40	kPa	283.13	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
Pvap	415.50	kPa	283.15	Vapor-liquid equilibria measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + isobutane (HC-600a) ternary system
Pvap	414.00	kPa	283.15	Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
Pvap	416.00	kPa	283.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	416.90	kPa	283.15	Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Pvap	414.30	kPa	283.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	414.60	kPa	283.15	Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
Pvap	416.60	kPa	283.15	Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
Pvap	414.60	kPa	283.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	413.80	kPa	283.15	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	415.40	kPa	283.16	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	415.71	kPa	283.16	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	415.71	kPa	283.17	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	414.30	kPa	283.17	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	407.20	kPa	283.22	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	416.70	kPa	283.24	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	428.70	kPa	284.10	PVTx properties in the gas phase for binary R290/R134a system
Pvap	442.10	kPa	285.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	445.40	kPa	285.26	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	472.30	kPa	287.15	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	475.40	kPa	287.27	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	487.00	kPa	288.09	PVTx properties in the gas phase for binary R290/R134a system
Pvap	488.20	kPa	288.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	488.20	kPa	288.16	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	488.40	kPa	288.17	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	483.60	kPa	288.30	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	503.40	kPa	289.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	506.90	kPa	289.27	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	536.30	kPa	291.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	539.90	kPa	291.29	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	554.10	kPa	292.13	PVTx properties in the gas phase for binary R290/R134a system
Pvap	569.00	kPa	292.90	Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
Pvap	569.00	kPa	292.90	Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap	571.00	kPa	292.92	Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
Pvap	570.90	kPa	293.14	Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
Pvap	571.10	kPa	293.14	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
Pvap	572.40	kPa	293.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	571.10	kPa	293.15	Experimental measurements and correlation of isothermal vapor-liquid equilibria for HFC-32 + HFO-1234ze (E) and HFC-134a + HFO-1234ze (E) binary systems
Pvap	572.10	kPa	293.15	Isothermal vapour + liquid equilibrium measurements and correlation for the pentafluoroethane + cyclopropane and the cyclopropane + 1,1,1,2-tetrafluoroethane binary systems
Pvap	570.60	kPa	293.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	572.00	kPa	293.15	Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
Pvap	572.40	kPa	293.15	Vapor-liquid equilibria measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + isobutane (HC-600a) ternary system
Pvap	571.50	kPa	293.15	Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
Pvap	571.90	kPa	293.15	Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Pvap	570.70	kPa	293.15	The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
Pvap	571.70	kPa	293.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	571.20	kPa	293.15	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	571.94	kPa	293.22	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	571.98	kPa	293.22	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	566.30	kPa	293.29	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	575.10	kPa	293.31	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	572.60	kPa	293.32	Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
Pvap	610.80	kPa	295.30	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	612.00	kPa	295.40	Solubility Measurements of 1,1,1,2-Tetrafluoroethane (R134a) and of Propane in Squalane at Temperatures from (325 to 400) K and Pressures from (0.1 to 1) MPa
Pvap	630.30	kPa	296.32	PVTx properties in the gas phase for binary R290/R134a system
Pvap	649.30	kPa	297.32	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	664.80	kPa	298.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	665.10	kPa	298.16	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	669.60	kPa	298.44	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	685.50	kPa	299.21	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	688.70	kPa	299.31	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	689.40	kPa	299.34	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	704.40	kPa	300.00	Solubility Measurements of 1,1,1,2-Tetrafluoroethane (R134a) and of Propane in Squalane at Temperatures from (325 to 400) K and Pressures from (0.1 to 1) MPa
Pvap	707.10	kPa	300.17	PVTx properties in the gas phase for binary R290/R134a system
Pvap	726.70	kPa	301.19	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	730.00	kPa	301.30	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	763.00	kPa	302.70	Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap	763.00	kPa	302.70	Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
Pvap	767.00	kPa	303.06	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	769.50	kPa	303.12	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
Pvap	769.20	kPa	303.12	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
Pvap	770.20	kPa	303.15	Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
Pvap	770.40	kPa	303.15	Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Pvap	770.20	kPa	303.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	769.20	kPa	303.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	768.90	kPa	303.15	Vapor-liquid equilibria measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + isobutane (HC-600a) ternary system
Pvap	771.50	kPa	303.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	771.40	kPa	303.15	Experimental measurements and correlation of isothermal vapor-liquid equilibria for HFC-32 + HFO-1234ze (E) and HFC-134a + HFO-1234ze (E) binary systems
Pvap	767.00	kPa	303.15	Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
Pvap	769.80	kPa	303.16	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	769.80	kPa	303.19	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	773.30	kPa	303.24	Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
Pvap	771.67	kPa	303.25	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	771.76	kPa	303.26	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	772.90	kPa	303.30	P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
Pvap	773.50	kPa	303.31	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	775.70	kPa	303.45	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	775.70	kPa	303.45	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	788.50	kPa	304.00	Solubility Measurements of 1,1,1,2-Tetrafluoroethane (R134a) and of Propane in Squalane at Temperatures from (325 to 400) K and Pressures from (0.1 to 1) MPa
Pvap	792.40	kPa	304.12	PVTx properties in the gas phase for binary R290/R134a system
Pvap	819.10	kPa	305.33	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	866.60	kPa	307.34	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	887.00	kPa	308.12	PVTx properties in the gas phase for binary R290/R134a system
Pvap	885.90	kPa	308.15	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	886.00	kPa	308.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	892.20	kPa	308.44	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	892.20	kPa	308.44	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	916.00	kPa	309.35	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	967.30	kPa	311.35	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	991.80	kPa	312.19	PVTx properties in the gas phase for binary R290/R134a system
Pvap	1002.20	kPa	312.66	Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
Pvap	1014.90	kPa	313.11	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
Pvap	1015.30	kPa	313.15	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	1008.00	kPa	313.15	Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
Pvap	1013.00	kPa	313.15	Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
Pvap	1012.80	kPa	313.15	Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Pvap	1015.50	kPa	313.15	Vapor-liquid equilibria measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + isobutane (HC-600a) ternary system
Pvap	1018.10	kPa	313.15	Experimental measurements and correlation of isothermal vapor-liquid equilibria for HFC-32 + HFO-1234ze (E) and HFC-134a + HFO-1234ze (E) binary systems
Pvap	1013.60	kPa	313.15	Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
Pvap	1017.00	kPa	313.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	1017.70	kPa	313.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	1018.80	kPa	313.15	P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
Pvap	1013.00	kPa	313.15	Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
Pvap	1017.50	kPa	313.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	1018.09	kPa	313.18	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	1018.15	kPa	313.18	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	1018.80	kPa	313.30	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	1018.80	kPa	313.30	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	1014.70	kPa	313.31	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	1019.30	kPa	313.31	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1076.90	kPa	315.36	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1103.50	kPa	316.20	PVTx properties in the gas phase for binary R290/R134a system
Pvap	1133.00	kPa	317.32	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1158.40	kPa	318.14	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	1158.10	kPa	318.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	1165.40	kPa	318.39	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	1165.40	kPa	318.39	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	1195.50	kPa	319.38	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1220.60	kPa	320.09	PVTx properties in the gas phase for binary R290/R134a system
Pvap	1256.10	kPa	321.34	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1304.90	kPa	322.82	Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
Pvap	1316.90	kPa	323.14	Experimental measurements and correlation of isothermal vapor-liquid equilibria for HFC-32 + HFO-1234ze (E) and HFC-134a + HFO-1234ze (E) binary systems
Pvap	1316.10	kPa	323.15	Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Pvap	1317.20	kPa	323.15	Vapor-liquid equilibria measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + isobutane (HC-600a) ternary system
Pvap	1318.80	kPa	323.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	1312.80	kPa	323.15	Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
Pvap	1314.70	kPa	323.15	Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
Pvap	1318.00	kPa	323.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	1319.00	kPa	323.15	P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
Pvap	1308.00	kPa	323.15	Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
Pvap	1313.80	kPa	323.15	Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Pvap	1308.00	kPa	323.15	Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
Pvap	1317.40	kPa	323.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	1318.50	kPa	323.17	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
Pvap	1319.76	kPa	323.19	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	1319.87	kPa	323.20	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	1319.00	kPa	323.30	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	1319.00	kPa	323.30	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	1487.96	kPa	328.05	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
Pvap	1489.60	kPa	328.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	1492.40	kPa	328.26	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	1492.40	kPa	328.26	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	1532.30	kPa	329.37	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1681.60	kPa	333.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	1671.00	kPa	333.15	Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
Pvap	1679.70	kPa	333.15	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	1673.00	kPa	333.15	Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
Pvap	1682.00	kPa	333.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	1681.10	kPa	333.16	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
Pvap	1682.95	kPa	333.16	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	1683.15	kPa	333.17	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	1683.70	kPa	333.30	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	1683.70	kPa	333.30	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	1680.40	kPa	333.32	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	1767.40	kPa	335.39	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1851.90	kPa	337.41	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	1889.10	kPa	338.14	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	1889.60	kPa	338.24	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	1889.60	kPa	338.24	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	1889.60	kPa	338.30	P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
Pvap	1939.20	kPa	339.41	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	2029.50	kPa	341.43	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	2110.59	kPa	343.03	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	2110.88	kPa	343.04	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	2118.10	kPa	343.14	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	2117.00	kPa	343.15	Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Pvap	2114.50	kPa	343.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	2106.00	kPa	343.15	Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
Pvap	2117.30	kPa	343.16	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
Pvap	2115.30	kPa	343.23	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	2115.30	kPa	343.23	p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
Pvap	2123.00	kPa	343.43	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	2319.80	kPa	347.44	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	2361.20	kPa	348.13	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	2352.50	kPa	348.22	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	2419.40	kPa	349.46	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	2530.30	kPa	351.46	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	2620.85	kPa	352.93	Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
Pvap	2605.90	kPa	353.10	Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Pvap	2634.60	kPa	353.13	Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
Pvap	2629.00	kPa	353.15	Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Pvap	2633.57	kPa	353.16	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	2633.73	kPa	353.16	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	2636.00	kPa	353.20	Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
Pvap	2605.90	kPa	353.45	P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
Pvap	2641.10	kPa	353.48	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	2755.40	kPa	355.48	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	3054.30	kPa	360.48	Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Pvap	3245.32	kPa	363.17	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap	3245.53	kPa	363.18	Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus

Datasets

1. Viscosity, Pa*s (4)
2. Mass density, kg/m3 (7)
3. Amount density, mol/m3 (1)
4. Self diffusion coefficient, m2/s (1)
5. Thermal conductivity, W/m/K (1)
6. Molar volume, m3/mol (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Viscosity, Pa*s - Fluid (supercritical or subcritical phases)
293.15	10000.00	0.0003
293.15	25000.00	0.0003
293.15	50000.00	0.0004
293.15	100000.00	0.0005
293.15	150000.00	0.0007
293.15	200000.00	0.0008
298.15	10000.00	0.0002
298.15	25000.00	0.0003
298.15	50000.00	0.0003
298.15	100000.00	0.0005
298.15	150000.00	0.0006
298.15	200000.00	0.0008
298.15	250000.00	0.0010
313.15	10000.00	0.0002
313.15	25000.00	0.0002
313.15	50000.00	0.0003
313.15	100000.00	0.0004
313.15	150000.00	0.0006
313.15	200000.00	0.0007
313.15	250000.00	0.0009
313.15	300000.00	0.0011
313.15	350000.00	0.0013
313.15	400000.00	0.0014
323.15	10000.00	0.0002
323.15	25000.00	0.0002
323.15	50000.00	0.0003
323.15	100000.00	0.0004
323.15	150000.00	0.0005
323.15	200000.00	0.0006
323.15	250000.00	0.0008
323.15	300000.00	0.0009
348.15	10000.00	0.0001
348.15	25000.00	0.0002
348.15	50000.00	0.0002
348.15	100000.00	0.0003
348.15	150000.00	0.0004
348.15	200000.00	0.0005
348.15	250000.00	0.0006
348.15	300000.00	0.0008
348.15	350000.00	0.0009
348.15	400000.00	0.0010
373.15	25000.00	0.0002
373.15	50000.00	0.0002
373.15	100000.00	0.0003
373.15	150000.00	0.0004
373.15	200000.00	0.0005
373.15	250000.00	0.0006
373.15	300000.00	0.0006
373.15	350000.00	0.0008
373.15	400000.00	0.0009
398.15	50000.00	0.0002
398.15	100000.00	0.0003
398.15	150000.00	0.0003
438.15	50000.00	0.0001
438.15	100000.00	0.0002
438.15	150000.00	0.0003
438.15	200000.00	0.0003
438.15	250000.00	0.0004
438.15	300000.00	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
253.14	1000.00	0.0004
253.14	5000.00	0.0004
253.14	10000.00	0.0004
253.14	15000.00	0.0004
253.14	20000.00	0.0004
253.14	25000.00	0.0005
253.14	30000.00	0.0005
273.15	1000.00	0.0003
273.15	5000.00	0.0003
273.15	10000.00	0.0003
273.15	15000.00	0.0003
273.15	20000.00	0.0003
273.15	25000.00	0.0004
273.15	30000.00	0.0004
293.15	1000.00	0.0002
293.15	5000.00	0.0002
293.15	10000.00	0.0002
293.15	15000.00	0.0003
293.15	20000.00	0.0003
293.15	25000.00	0.0003
293.15	30000.00	0.0003
313.14	2000.00	0.0002
313.14	5000.00	0.0002
313.14	10000.00	0.0002
313.14	15000.00	0.0002
313.14	20000.00	0.0002
313.14	25000.00	0.0002
313.14	30000.00	0.0003
333.16	2000.00	0.0001
333.16	5000.00	0.0001
333.16	10000.00	0.0002
333.16	15000.00	0.0002
333.16	20000.00	0.0002
333.16	25000.00	0.0002
333.16	30000.00	0.0002
353.16	3000.00	0.0001
353.16	5000.00	0.0001
353.16	10000.00	0.0001
353.16	15000.00	0.0001
353.16	20000.00	0.0002
353.16	25000.00	0.0002
353.16	30000.00	0.0002
253.16	3000.00	0.0004
253.16	10000.00	0.0004
273.15	3000.00	0.0003
273.15	10000.00	0.0003
293.15	3000.00	0.0002
293.15	10000.00	0.0002
313.14	3000.00	0.0002
313.14	10000.00	0.0002
333.16	3000.00	0.0001
333.16	10000.00	0.0002
353.15	5000.00	0.0001
353.15	10000.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
313.50	1796.00	0.0002
313.01	1763.00	0.0002
312.96	1701.00	0.0002
312.83	1706.00	0.0002
312.82	4048.00	0.0002
312.76	4069.00	0.0002
312.75	4064.00	0.0002
312.77	3061.00	0.0002
312.78	3061.00	0.0002
312.78	3042.00	0.0002
332.81	4011.00	0.0001
332.81	4008.00	0.0001
332.80	4005.00	0.0001
332.80	3079.00	0.0001
332.79	3083.00	0.0001
332.79	3072.00	0.0001
354.96	4007.00	0.0001
355.51	4078.00	0.0001
355.94	4155.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
258.15	1000.00	0.0003
258.15	5000.00	0.0003
258.15	10000.00	0.0004
258.15	15000.00	0.0004
258.15	20000.00	0.0004
258.15	25000.00	0.0004
258.15	30000.00	0.0005
258.15	35000.00	0.0005
258.15	40000.00	0.0005
278.14	1000.00	0.0003
278.14	5000.00	0.0003
278.14	10000.00	0.0003
278.14	15000.00	0.0003
278.14	20000.00	0.0003
278.14	25000.00	0.0003
278.14	30000.00	0.0004
278.14	35000.00	0.0004
278.14	40000.00	0.0004
298.14	1000.00	0.0002
298.14	5000.00	0.0002
298.14	10000.00	0.0002
298.14	15000.00	0.0002
298.14	20000.00	0.0003
298.14	25000.00	0.0003
298.14	30000.00	0.0003
298.14	35000.00	0.0003
298.14	40000.00	0.0003
318.13	2000.00	0.0002
318.13	5000.00	0.0002
318.13	10000.00	0.0002
318.13	15000.00	0.0002
318.13	20000.00	0.0002
318.13	25000.00	0.0002
318.13	30000.00	0.0002
318.13	35000.00	0.0003
318.13	40000.00	0.0003
338.13	2000.00	0.0001
338.13	5000.00	0.0001
338.13	10000.00	0.0001
338.13	15000.00	0.0002
338.13	20000.00	0.0002
338.13	25000.00	0.0002
338.13	30000.00	0.0002
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.26	1000.00	1188.74
283.52	1010.00	1262.83
323.07	1280.00	1102.44
343.05	2090.00	997.14
343.03	4990.00	1045.24
303.27	5000.00	1212.6
323.08	5000.00	1136.68
362.95	5000.00	921.91
283.53	5000.00	1279.7
283.54	10000.00	1298.2
323.08	10000.00	1170.98
343.02	10000.00	1097.0
362.95	10000.00	1012.79
303.28	10000.00	1237.15
303.29	19980.00	1275.91
283.54	20000.00	1329.16
343.02	20000.00	1162.16
362.96	20000.00	1101.23
323.09	20000.00	1220.67
343.02	39990.00	1241.93
283.54	39990.00	1376.78
362.97	40000.00	1196.59
323.12	40000.00	1287.6
303.29	40010.00	1332.33
323.11	60000.00	1335.02
362.98	60000.00	1257.2
303.30	60000.00	1374.15
343.02	60010.00	1295.73
283.54	60010.00	1413.66
303.30	79980.00	1408.2
323.11	80000.00	1372.84
362.99	80000.00	1302.95
343.03	80010.00	1337.58
283.54	80020.00	1444.29
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.26	1000.00	1265.88
283.26	5000.00	1282.35
283.26	10000.00	1300.86
283.26	20000.00	1331.64
283.26	40000.00	1379.61
283.25	60000.00	1416.44
283.26	80000.00	1446.35
302.85	1000.00	1190.34
302.85	5000.00	1214.03
302.85	10000.00	1238.45
302.84	20000.00	1276.99
302.84	40000.00	1333.11
302.85	60000.00	1374.79
302.84	80000.00	1408.64
322.62	5000.00	1140.59
322.63	10000.00	1174.6
322.63	20000.00	1224.02
322.64	40000.00	1290.68
322.64	60000.00	1338.04
322.64	80000.00	1375.39
342.56	5000.00	1047.23
342.56	10000.00	1098.48
342.56	20000.00	1163.35
342.56	40000.00	1242.84
342.57	60000.00	1296.48
342.57	80000.00	1337.6
362.57	5000.00	924.58
362.58	10000.00	1014.86
362.58	20000.00	1102.88
362.58	40000.00	1197.86
362.58	60000.00	1258.31
362.58	80000.00	1303.78
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.27	1010.00	1188.92
303.27	5010.00	1212.9
303.26	10020.00	1237.53
303.26	20020.00	1276.18
303.27	40000.00	1332.27
303.27	59990.00	1374.03
303.29	79930.00	1408.19
322.47	5000.00	1139.41
322.48	10000.00	1173.46
322.48	19990.00	1222.36
322.48	40000.00	1289.13
322.48	60010.00	1336.26
322.48	80000.00	1373.47
342.86	5010.00	1045.93
342.87	10010.00	1097.7
342.88	20010.00	1162.75
342.89	40000.00	1242.46
342.89	60010.00	1296.15
342.89	80000.00	1337.87
362.81	5000.00	921.95
362.82	10010.00	1013.37
362.83	20010.00	1101.82
362.83	40010.00	1197.04
362.84	60000.00	1257.56
362.84	79990.00	1303.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.61	1000.00	1262.74
283.61	5000.00	1279.71
283.61	10000.00	1298.25
283.61	20000.00	1329.21
283.59	40000.00	1376.92
283.59	60000.00	1413.86
283.60	80000.00	1444.35
303.46	1000.00	1188.35
303.46	5000.00	1212.37
303.46	10000.00	1237.01
303.46	20000.00	1275.97
303.46	40000.00	1332.37
303.47	60000.00	1374.37
303.47	80000.00	1408.33
323.24	3000.00	1119.53
323.24	5000.00	1136.67
323.24	10000.00	1171.08
323.24	20000.00	1220.9
323.24	40000.00	1287.9
323.24	60000.00	1335.45
323.25	80000.00	1373.28
343.03	3000.00	1015.76
343.01	5000.00	1046.15
343.02	10000.00	1098.02
343.02	20000.00	1163.58
343.03	40000.00	1243.36
343.03	60000.00	1297.19
343.03	80000.00	1338.42
362.73	5000.00	923.63
362.75	10000.00	1014.58
362.75	20000.00	1102.91
362.75	40000.00	1198.13
362.74	60000.00	1258.69
362.74	80000.00	1304.07
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.46	1000.00	1262.57
283.46	5000.00	1279.58
283.47	10000.00	1298.12
283.47	20000.00	1329.18
283.47	40000.00	1377.11
283.47	60000.00	1414.44
283.47	80000.00	1445.46
303.38	1000.00	1188.07
303.38	5000.00	1212.13
303.37	10000.00	1236.85
303.37	20000.00	1275.77
303.38	40000.00	1332.36
303.38	60000.00	1374.64
303.38	80000.00	1408.98
323.15	3000.00	1119.19
323.16	5000.00	1136.38
323.16	10000.00	1170.84
323.16	20000.00	1220.65
323.16	40000.00	1287.71
323.16	60000.00	1335.49
323.16	80000.00	1373.39
342.97	3000.00	1014.76
342.97	5000.00	1045.25
342.98	10000.00	1097.42
342.98	20000.00	1162.91
342.98	40000.00	1242.75
342.99	60000.00	1296.65
342.98	80000.00	1338.34
362.68	5000.00	922.4
362.68	10000.00	1013.83
362.68	20000.00	1102.6
362.68	40000.00	1197.86
362.68	60000.00	1258.47
362.68	80000.00	1304.15
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.57	5000.00	1279.4
283.57	10000.00	1297.9
283.56	20000.00	1328.7
283.55	40000.00	1376.3
283.55	60000.00	1413.1
283.55	80000.00	1443.2
303.39	1000.00	1188.5
303.39	5000.00	1212.5
303.39	10000.00	1237.0
303.39	20000.00	1275.9
303.39	40000.00	1332.1
303.40	60000.00	1373.9
303.39	80000.00	1407.4
322.89	3000.00	1120.9
322.91	5000.00	1137.8
322.91	10000.00	1172.0
322.93	20000.00	1221.5
322.93	40000.00	1288.4
322.93	60000.00	1335.8
322.94	80000.00	1372.8
342.75	3000.00	1017.4
342.75	5000.00	1047.5
342.76	10000.00	1098.8
342.77	20000.00	1164.1
342.77	40000.00	1243.6
342.78	60000.00	1297.3
342.78	80000.00	1338.2
362.57	5000.00	924.9
362.57	10000.00	1015.4
362.58	20000.00	1103.4
362.59	40000.00	1198.4
362.59	60000.00	1258.8
362.59	80000.00	1303.8
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
5000.00	308.00	1150.0
10100.00	308.00	1180.0
15400.00	308.00	1210.0
19600.00	288.00	1290.0
19600.00	298.00	1270.0
19600.00	308.00	1240.0
19600.00	318.00	1210.0
19600.00	328.00	1180.0
19600.00	308.00	1240.0
23700.00	308.00	1260.0
Reference

Amount density, mol/m3

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Amount density, mol/m3 - Gas
353.17	1761.50	776.7
353.17	1359.70	555.7
353.17	1026.00	397.6
353.17	762.10	284.5
353.17	559.90	203.6
353.17	408.20	145.7
353.17	296.00	104.2
353.17	213.80	74.57
413.17	2606.80	918.8
413.17	1968.80	657.4
413.17	1464.60	470.4
413.17	1077.60	336.6
413.17	786.70	240.8
413.17	571.00	172.3
413.17	412.80	123.3
413.17	297.50	88.22
413.17	214.00	63.12
Reference

Self diffusion coefficient, m2/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Self diffusion coefficient, m2/s - Liquid
670.00	298.15	0.0000
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Thermal conductivity, W/m/K - Fluid (supercritical or subcritical phases)
299.29	170.00	0.0129
299.63	170.00	0.0128
318.97	740.00	0.0149
318.97	740.00	0.0149
319.14	160.00	0.0146
345.58	180.00	0.0171
346.36	180.00	0.0174
348.54	180.00	0.0173
351.84	640.00	0.0176
363.88	180.00	0.0189
365.00	180.00	0.0189
365.41	180.00	0.0189
365.69	180.00	0.0189
366.52	180.00	0.0189
366.80	180.00	0.0189
372.42	680.00	0.0198
372.43	170.00	0.0197
372.43	680.00	0.0197
378.07	180.00	0.0200
378.63	440.00	0.0202
378.74	180.00	0.0201
378.90	330.00	0.0203
379.17	300.00	0.0202
379.43	150.00	0.0204
379.72	160.00	0.0200
392.65	180.00	0.0214
426.86	160.00	0.0247
436.44	180.00	0.0254
446.25	200.00	0.0267
446.25	760.00	0.0266
451.17	180.00	0.0268
455.69	100.00	0.0268
455.92	680.00	0.0272
466.31	650.00	0.0285
476.24	100.00	0.0292
496.18	100.00	0.0311
515.97	100.00	0.0330
Reference

Molar volume, m3/mol

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Molar volume, m3/mol - Gas
253.09	107.60	0.0187
272.92	158.90	0.0136
282.69	329.10	0.0065
282.80	121.40	0.0188
292.87	171.90	0.0136
292.89	126.20	0.0188
302.58	357.70	0.0065
313.10	135.40	0.0188
313.10	184.90	0.0136
323.07	386.50	0.0065
333.03	144.30	0.0188
333.03	1610.80	0.0012
333.05	197.50	0.0136
342.96	413.70	0.0065
343.00	1706.90	0.0012
352.93	153.20	0.0188
352.94	1798.60	0.0012
353.04	210.00	0.0136
362.89	440.70	0.0065
362.90	1888.60	0.0012
372.82	454.00	0.0065
372.84	162.10	0.0188
372.87	1976.60	0.0013
372.99	222.40	0.0136
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.69; 3482.14]	kPa	[172.00; 374.21]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.41969e+01
Coefficient B			-2.08778e+03
Coefficient C			-2.86360e+01
Temperature range, min.			172.00
Temperature range, max.			374.21
Pvap	0.69	kPa	172.00	Calculated Property
Pvap	4.99	kPa	194.47	Calculated Property
Pvap	22.41	kPa	216.94	Calculated Property
Pvap	73.06	kPa	239.40	Calculated Property
Pvap	189.71	kPa	261.87	Calculated Property
Pvap	416.55	kPa	284.34	Calculated Property
Pvap	805.52	kPa	306.81	Calculated Property
Pvap	1411.49	kPa	329.27	Calculated Property
Pvap	2287.69	kPa	351.74	Calculated Property
Pvap	3482.14	kPa	374.21	Calculated Property
Pvap	[0.72; 4272.46]	kPa	[172.15; 380.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			4.84910e+01
Coefficient B			-3.73115e+03
Coefficient C			-5.32695e+00
Coefficient D			9.21593e-06
Temperature range, min.			172.15
Temperature range, max.			380.00
Pvap	0.72	kPa	172.15	Calculated Property
Pvap	5.14	kPa	195.24	Calculated Property
Pvap	23.34	kPa	218.34	Calculated Property
Pvap	77.26	kPa	241.43	Calculated Property
Pvap	203.87	kPa	264.53	Calculated Property
Pvap	455.62	kPa	287.62	Calculated Property
Pvap	899.45	kPa	310.72	Calculated Property
Pvap	1616.20	kPa	333.81	Calculated Property
Pvap	2702.02	kPa	356.91	Calculated Property
Pvap	4272.46	kPa	380.00	Calculated Property

Similar Compounds

Find more compounds similar to Norflurane.

Mixtures

• Norflurane + Dimethyl ether
• Propane + Norflurane
• 2,5,8,11-Tetraoxadodecane + Norflurane
• Difluoromethane + Norflurane
• Cyclopropane + Norflurane
• Ethane, hexafluoro- + Norflurane
• Ethane, 1,2-dimethoxy- + Norflurane
• 3,3,3-Trifluoropropene + Norflurane
• Ammonia + Norflurane
• Norflurane + Propane, 1,1,1,3,3-pentafluoro
• N,N-Dimethylacetamide + Norflurane
• 2-Pyrrolidinone, 1-methyl- + Norflurane
• Butane + Norflurane
• CF3OCH3 + Norflurane
• Squalane + Norflurane
• Norflurane + Perfluoropropane + Isobutane
• Ethane, pentafluoro- + Butane + Norflurane
• Ethane, fluoro- + Norflurane
• Proline + Norflurane
• Formamide, N,N-dimethyl- + Norflurane

Find more mixtures with Norflurane.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• High-Pressure Viscosity Measurements of 1,1,1,2-Tetrafluoroethane
• Thermophysical Properties of the Refrigerant Mixtures R417A and R417B from Dynamic Light Scattering (DLS)
• Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
• Viscosity measurements and correlations of binary mixtures: 1,1,1,2-tetrafluoroethane (HFC-134a) + tetraethylene glycol dimethylether (TEGDME)
• Solubility and diffusivity of 1,1,1,2-tetrafluoroethane in room-temperature ionic liquids
• Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
• Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
• High-pressure viscosity behavior of x 1,1,1,2-tetrafluoroethane (HFC-134a) + (1-x) triethylene glycol dimethylether (TriEGDME) mixtures: Measurements and modeling
• Vapor liquid equilibria and critical loci of binary and ternary systems composed of CH2F2, C2HF5 and C2H2F4
• Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
• Isothermal vapour + liquid equilibrium measurements and correlation for the pentafluoroethane + cyclopropane and the cyclopropane + 1,1,1,2-tetrafluoroethane binary systems
• Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
• Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
• Phase equilibria of imidazolium ionic liquids and the refrigerant gas, 1,1,1,2-tetrafluoroethane (R-134a)
• Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-134a
• Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
• An experimental study of PVTx properties in the gas phase for binary mixtures of HFO-1234yf and HFC-134a
• Gaseous absorption of fluorinated ethanes by ionic liquids
• Surface tension and liquid viscosity measurement for binary mixtures of R134a with R1234yf and R1234ze(E)
• Vapor-liquid equilibria measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + isobutane (HC-600a) ternary system
• Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
• Viscosity and self-diffusivity of ionic liquids with compressed hydrofluorocarbons: 1-hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)amide and 1,1,1,2- tetrafluoroethane.
• Solubility of cinnamic acid in supercritical carbon dioxide and subcritical 1,1,1,2-tetrafluoroethane: Experimental data and modelling
• Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
• Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
• Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
• Density measurements for 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
• Viscosity measurements for 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
• Liquid density of HFE-7200 and HFE-7500 from T = (283 to 363) K at pressures up to 100 MPa
• PVTx properties in the gas phase for binary R290/R134a system
• Liquid density of HFE-7000 and HFE-7100 from T = (283 to 363) K at pressures up to 100 MPa
• Gaseous pVTx measurements for (HFC134a + HC290) by a compact single-sinker densimeter
• (Vapour + liquid + liquid) equilibrium measurements and correlation for the {1,1,1,2-tetrafluoroethane (R134a) + n-butane (R600)} system
• Volumetric properties of binary mixtures of {difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))} at temperatures from 283.15 K to 363.15 K and pressures up to 100 MPa
• The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
• Measurements of isothermal vapor-liquid equilibrium for 2,3,3,3-tetrafluoroprop-1-ene + 1,1,1,2-tetrafluoroethane + propane system at temperatures from 283.15 to 323.15 K
• Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
• P.rho.Tx properties of binary R134a/R245fa system
• Experimental measurements and correlation of isothermal vapor-liquid equilibria for HFC-32 + HFO-1234ze (E) and HFC-134a + HFO-1234ze (E) binary systems
• Solubilities of hydroxybenzaldehyde isomers and their mixture in subcritical 1,1,1,2-tetrafluoroethane
• Liquid Density of 2 Methoxyethyl Acetate, 2 Ethylhexyl Acetate and Diethyl Succinate at Temperatures from 283.15 K to 363.15 K and Pressures up to 100 MPa
• Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
• P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
• Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + Dimethyl Ether Triethylene Glycol, 1,1-Difluoroethane + Dimethyl Ether Triethylene Glycol, and 1,1-Difluoroethane + N-Methyl-2-pyrrolidone Systems
• Experimental Study of PVTx Properties in the Gas Phase for Binary Mixtures of DME and HFC-134a
• Gaseous PVT Property Measurements of cis-1,3,3,3-Tetrafluoropropene
• Measurement and Correlation of Vapor-Liquid Equilibrium for R124 (1-Chloro-1,2,2,2-Tetrafluoroethane)-NMP (N-Methyl-2-Pyrrolidone) and R124-DMF (N,N-Dimethylformamide) Mixtures
• Measurement of Viscosity of cis-1,1,1,4,4,4-Hexafluoro-2-butene (R-1336mzz(Z)) by Tandem Capillary Tubes Method
• Liquid Density of n-Pentene, n-Hexene, and n-Heptene at Temperatures from 283.15 to 363.15 K and Pressures up to 100 MPa
• Measurement and Correlation of the Solubilities of Azoxystrobin, Flutriafol, and Tebuconazole in Subcritical 1,1,1,2-Tetrafluoroethane
• Critical Parameters and Vapor Pressures Measurements of Hydrofluoroethers at High Temperatures
• Surface Tension Measurements of Difluoromethane(R-32) and the Binary Mixture Difluoromethane(R-32) + 1,1,1,2-tetrafluoroethane(R-134a) from (253 to 333) K
• Surface Tension for the 1,1,1-Trifluoroethane (R-143a) + 1,1,1,2-Tetrafluoroethane (R-134a) System
• Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
• Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
• Critical Parameters Measurements of Four HFE + HFC Binary Systems: Pentafluoromethoxyethane (HFE-245Mc) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
• Critical Properties of Four HFE + HFC Binary Systems: Trifluoromethoxymethane (HFE-143m) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
• P-rho-T-x Measurements for (1,1,1,2-Tetrafluoroethane + Triethylene Glycol Dimethyl Ether) at High Haloalkane Content
• Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
• Acoustic Determination of Thermophysical Properties and Critical Parameters for R404A and Critical Line of xCO2 + (1 - x)R404A
• Solubility and Phase Behaviors of AOT Analogue Surfactants in 1,1,1,2-Tetrafluoroethane and Supercritical Carbon Dioxide
• Vapor-Liquid Equilibria for the Trifluoromethane + 1,1,1,2-Tetrafluoroethane System
• Vapor-Liquid-Liquid Equilibria of Hydrofluorocarbons + 1-Butyl-3-methylimidazolium Hexafluorophosphate
• Solubility Measurements of 1,1,1,2-Tetrafluoroethane (R134a) and of Propane in Squalane at Temperatures from (325 to 400) K and Pressures from (0.1 to 1) MPa
• P-V-T Behavior of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf) in the Vapor Phase from (243 to 373) K
• Solubility of Refrigerant 1,1,1,2-Tetrafluoroethane in the N,N-Dimethyl Formamide in the Temperature Range from (263.15 to 363.15) K
• Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
• Compressed Liquid Viscosity of 1,1,1,3,3-Pentafluoropropane (R245fa) and 1,1,1,3,3,3-Hexafluoropropane (R236fa)
• Isochoric PVTx Measurements for the Carbon Dioxide + 1,1,1,2-Tetrafluoroethane Binary System
• Experimental Study of p-.rho.-T Relationship of Compressed Liquid Phase for Octafluoropropane and Two near Azeotropic Ternary HFC/HC Mixtures
• Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + N,N-Dimethylacetamide, Fluoroethane + N-Methyl-2-pyrrolidone, and 1,1,1,2-Tetrafluoroethane + N,N-Dimethylacetamide Systems
• Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
• Investigation on liquid density data at the bubble point and equations for the refrigerant HFC-404A over a wide temperature range
• Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
• Solubility of 4-Aminosalicylic Acid in Supercritical Carbon Dioxide and Subcritical 1,1,1,2-Tetrafluoroethane
• Isothermal Vapor-liquid Equilibrium of the ternary mixture of 1,1,1,2-tetrafluoroethane + 2,3,3,3-tetrafluoroprop-1- ene + dimethylether at temperatures from 253.15 to 323.15 K
• Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
• Solubility Differences of Halocarbon Isomers in Ionic Liquid [emim][Tf2N]
• Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
• Solubilities of L-Proline in Subcritical HFC-134a and Supercritical CO2 Fluids
• Solubility of HFC134a (1,1,1,2-Tetrafluoroethane) in Two Dialkyl Carbonates
• Measurements of the Thermal Conductivity of HFC-134a in the Supercritical Region
• Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
• Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
• Kinematic Viscosity of R410A and R407C Refrigerant-Oil Mixtures in the Saturated Liquid Phase with Lubricant Mass Fraction in the Range of (0 to 0.0001)
• p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.