Chemical Properties of Ethane (CAS 74-84-0)

InChI

InChI=1S/C2H6/c1-2/h1-2H3

InChI Key

OTMSDBZUPAUEDD-UHFFFAOYSA-N

Formula

C2H6

SMILES

CC

Molecular Weight¹

30.07

CAS

74-84-0

Other Names

• Bimethyl
• C2H6
• Dimethyl
• Ethyl hydride
• Methylmethane
• R-170
• UN 1035
• UN 1961

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (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_subH : Enthalpy of sublimation 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).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_g : Gas Density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• 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	0.0990		KDB
PAff	596.30	kJ/mol	NIST
Tig	777.59	K	KDB
BasG	569.90	kJ/mol	NIST
ΔcH°gas	[-1560.70; -1559.80]	kJ/mol
ΔcH°gas	-1560.70 ± 0.30	kJ/mol	NIST
ΔcH°gas	-1559.90 ± 0.46	kJ/mol	NIST
ΔcH°gas	-1559.80 ± 0.46	kJ/mol	NIST
μ	0.00	debye	KDB
LFL	2.90	% in Air	KDB
UFL	13.00	% in Air	KDB
Tflash,cc	138.15	K	KDB
Tflash,oc	138.15	K	KDB
ΔfG°	-32.95	kJ/mol	KDB
Rg	1.8310		KDB
Δc,grossH	1550.42	kJ/mol	KDB
Δc,netH	1418.376	kJ/mol	KDB
ΔfH°gas	[-84.74; -83.80]	kJ/mol
ΔfH°gas	-84.74	kJ/mol	KDB
ΔfH°gas	-84.00 ± 0.40	kJ/mol	NIST
ΔfH°gas	-83.80 ± 0.30	kJ/mol	NIST
ΔfH°gas	-84.67 ± 0.49	kJ/mol	NIST
ΔfusH°	0.94	kJ/mol	Joback Calculated Property
ΔvapH°	9.76	kJ/mol	NIST
IE	[11.00; 12.10]	eV
IE	11.52 ± 0.04	eV	NIST
IE	Outlier 11.00 ± 1.00	eV	NIST
IE	11.52	eV	NIST
IE	11.57	eV	NIST
IE	11.56 ± 0.02	eV	NIST
IE	11.40 ± 0.40	eV	NIST
IE	11.50 ± 0.10	eV	NIST
IE	11.56 ± 0.02	eV	NIST
IE	11.76 ± 0.05	eV	NIST
IE	11.45 ± 0.05	eV	NIST
IE	11.51	eV	NIST
IE	11.66 ± 0.05	eV	NIST
IE	11.55	eV	NIST
IE	11.56	eV	NIST
IE	11.52 ± 0.01	eV	NIST
IE	11.99	eV	NIST
IE	12.00	eV	NIST
IE	12.10 ± 0.10	eV	NIST
IE	12.00	eV	NIST
log10WS	[-1.64; -1.36]
log10WS	-1.64		Aq. Solubility Prediction
log10WS	-1.36		Estimated Solubility
logPoct/wat	1.026		Crippen Calculated Property
McVol	39.040	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	1		KDB
Pc	[4580.00; 5100.00]	kPa
Pc	4872.00	kPa	KDB
Pc	4870.00 ± 10.00	kPa	NIST
Pc	4879.00 ± 13.79	kPa	NIST
Pc	4871.80 ± 10.00	kPa	NIST
Pc	4880.00	kPa	NIST
Pc	4877.00 ± 5.00	kPa	NIST
Pc	4889.00 ± 4.88	kPa	NIST
Pc	4871.43 ± 0.10	kPa	NIST
Pc	4889.00 ± 5.00	kPa	NIST
Pc	4778.00 ± 40.00	kPa	NIST
Pc	4871.40 ± 10.00	kPa	NIST
Pc	4871.80 ± 0.48	kPa	NIST
Pc	4884.00 ± 10.13	kPa	NIST
Pc	4875.00 ± 1.00	kPa	NIST
Pc	4930.00 ± 50.66	kPa	NIST
Pc	5044.00 ± 202.65	kPa	NIST
Pc	4876.00 ± 27.58	kPa	NIST
Pc	4875.00 ± 27.58	kPa	NIST
Pc	4920.00 ± 50.66	kPa	NIST
Pc	4910.00 ± 13.78	kPa	NIST
Pc	4884.00 ± 40.53	kPa	NIST
Pc	4910.00 ± 137.89	kPa	NIST
Pc	4951.00 ± 82.73	kPa	NIST
Pc	4877.00 ± 101.33	kPa	NIST
Pc	4950.00 ± 202.65	kPa	NIST
Pc	4954.79 ± 50.66	kPa	NIST
Pc	4907.00 ± 202.65	kPa	NIST
Pc	Outlier 5090.00 ± 202.65	kPa	NIST
Pc	Outlier 5100.00 ± 405.30	kPa	NIST
Pc	Outlier 4580.00 ± 303.98	kPa	NIST
Ptriple	1.10e-03 ± 5.00e-07	kPa	NIST
ρc	[200.89; 220.03]	kg/m3
ρc	206.57 ± 0.30	kg/m3	NIST
ρc	206.87 ± 3.01	kg/m3	NIST
ρc	202.97	kg/m3	NIST
ρc	200.89 ± 9.02	kg/m3	NIST
ρc	204.46 ± 3.01	kg/m3	NIST
ρc	205.79 ± 3.01	kg/m3	NIST
ρc	206.21 ± 3.01	kg/m3	NIST
ρc	205.49 ± 3.01	kg/m3	NIST
ρc	206.60 ± 0.21	kg/m3	NIST
ρc	206.21 ± 3.01	kg/m3	NIST
ρc	205.10 ± 3.01	kg/m3	NIST
ρc	202.97	kg/m3	NIST
ρc	214.99 ± 9.02	kg/m3	NIST
ρc	201.91 ± 6.01	kg/m3	NIST
ρc	Outlier 220.03 ± 9.02	kg/m3	NIST
ρc	202.97 ± 6.01	kg/m3	NIST
ρc	Outlier 220.02 ± 1.59	kg/m3	NIST
ρc	211.99 ± 6.01	kg/m3	NIST
ρc	206.87 ± 3.01	kg/m3	NIST
S°liquid	126.70	J/mol×K	NIST
Tboil	[184.10; 185.15]	K
Tboil	184.50	K	KDB
Tboil	184.46	K	NIST
Tboil	184.60 ± 0.20	K	NIST
Tboil	184.50 ± 0.30	K	NIST
Tboil	184.60	K	NIST
Tboil	184.50 ± 0.30	K	NIST
Tboil	184.52 ± 0.10	K	NIST
Tboil	184.55 ± 0.50	K	NIST
Tboil	184.65 ± 1.00	K	NIST
Tboil	184.60 ± 0.50	K	NIST
Tboil	184.30 ± 0.50	K	NIST
Tboil	185.15 ± 2.00	K	NIST
Tboil	184.30 ± 0.50	K	NIST
Tboil	185.15 ± 2.00	K	NIST
Tboil	184.10 ± 0.20	K	NIST
Tboil	184.85 ± 0.50	K	NIST
Tboil	184.85 ± 0.50	K	NIST
Tboil	184.15 ± 1.00	K	NIST
Tboil	185.15 ± 2.00	K	NIST
Tboil	184.46	K	NIST
Tboil	184.65 ± 0.50	K	NIST
Tboil	184.55 ± 0.50	K	NIST
Tboil	184.90 ± 1.50	K	NIST
Tboil	184.65 ± 0.50	K	NIST
Tc	[304.26; 308.20]	K
Tc	305.39	K	Surface tension and critical point measurements of methane + propane mixtures
Tc	305.32	K	KDB
Tc	305.32 ± 0.04	K	NIST
Tc	305.37 ± 0.10	K	NIST
Tc	305.32 ± 0.10	K	NIST
Tc	305.33 ± 0.10	K	NIST
Tc	305.42	K	NIST
Tc	305.39 ± 0.10	K	NIST
Tc	305.61 ± 0.03	K	NIST
Tc	305.34 ± 0.05	K	NIST
Tc	305.61 ± 0.10	K	NIST
Tc	305.40	K	NIST
Tc	305.38 ± 0.10	K	NIST
Tc	305.32 ± 0.10	K	NIST
Tc	305.37 ± 0.02	K	NIST
Tc	305.37 ± 0.02	K	NIST
Tc	305.34 ± 0.10	K	NIST
Tc	305.22 ± 0.20	K	NIST
Tc	305.36 ± 0.10	K	NIST
Tc	305.33 ± 0.03	K	NIST
Tc	305.35	K	NIST
Tc	305.35 ± 0.10	K	NIST
Tc	305.30 ± 0.03	K	NIST
Tc	305.35 ± 0.05	K	NIST
Tc	305.49 ± 0.40	K	NIST
Tc	305.33 ± 0.10	K	NIST
Tc	305.30	K	NIST
Tc	305.60	K	NIST
Tc	305.50 ± 0.40	K	NIST
Tc	305.47 ± 0.20	K	NIST
Tc	305.34 ± 0.10	K	NIST
Tc	305.10 ± 0.44	K	NIST
Tc	305.32 ± 0.10	K	NIST
Tc	Outlier 304.26 ± 0.40	K	NIST
Tc	305.47 ± 0.40	K	NIST
Tc	305.30 ± 0.20	K	NIST
Tc	305.00 ± 0.40	K	NIST
Tc	305.38 ± 0.20	K	NIST
Tc	305.42 ± 0.20	K	NIST
Tc	305.00 ± 0.55	K	NIST
Tc	306.00 ± 0.33	K	NIST
Tc	305.47 ± 0.60	K	NIST
Tc	305.25 ± 0.60	K	NIST
Tc	305.31 ± 1.00	K	NIST
Tc	305.10 ± 0.60	K	NIST
Tc	Outlier 307.00 ± 2.00	K	NIST
Tc	Outlier 307.70 ± 2.00	K	NIST
Tc	Outlier 308.20 ± 3.00	K	NIST
Tfus	[89.20; 101.00]	K
Tfus	90.30	K	KDB
Tfus	90.36	K	Aq. Solubility Prediction
Tfus	101.00 ± 1.00	K	NIST
Tfus	89.20 ± 1.50	K	NIST
Ttriple	[89.50; 101.00]	K
Ttriple	90.34 ± 0.01	K	NIST
Ttriple	90.35 ± 0.00	K	NIST
Ttriple	90.34 ± 0.02	K	NIST
Ttriple	90.34 ± 0.01	K	NIST
Ttriple	89.89 ± 0.10	K	NIST
Ttriple	90.35 ± 0.20	K	NIST
Ttriple	89.87 ± 0.02	K	NIST
Ttriple	89.55 ± 0.10	K	NIST
Ttriple	89.50 ± 0.15	K	NIST
Ttriple	Outlier 101.00 ± 0.30	K	NIST
Vc	[0.145; 0.148]	m3/kmol
Vc	0.145	m3/kmol	KDB
Vc	0.145	m3/kmol	NIST
Vc	0.145 ± 0.050	m3/kmol	NIST
Vc	0.146	m3/kmol	NIST
Vc	0.148 ± 0.001	m3/kmol	NIST
Vc	0.147 ± 0.001	m3/kmol	NIST
Vc	0.148	m3/kmol	NIST
Zc	0.2792400		KDB
Zra	0.28		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[41.66; 90.46]	J/mol×K	[189.20; 603.25]
Cp,gas	41.66 ± 0.31	J/mol×K	189.20	NIST
Cp,gas	43.25 ± 0.32	J/mol×K	209.30	NIST
Cp,gas	45.08 ± 0.34	J/mol×K	229.65	NIST
Cp,gas	47.27 ± 0.35	J/mol×K	249.90	NIST
Cp,gas	47.17 ± 0.35	J/mol×K	250.15	NIST
Cp,gas	49.68 ± 0.37	J/mol×K	272.00	NIST
Cp,gas	49.51 ± 0.04	J/mol×K	272.07	NIST
Cp,gas	50.66 ± 0.42	J/mol×K	279.00	NIST
Cp,gas	52.14 ± 0.39	J/mol×K	292.00	NIST
Cp,gas	53.27 ± 0.07	J/mol×K	302.70	NIST
Cp,gas	57.40 ± 0.04	J/mol×K	335.82	NIST
Cp,gas	58.91	J/mol×K	347.65	NIST
Cp,gas	60.38	J/mol×K	359.75	NIST
Cp,gas	61.04 ± 0.10	J/mol×K	364.78	NIST
Cp,gas	62.10 ± 0.47	J/mol×K	373.60	NIST
Cp,gas	63.89	J/mol×K	387.55	NIST
Cp,gas	72.43	J/mol×K	451.95	NIST
Cp,gas	80.08	J/mol×K	520.55	NIST
Cp,gas	86.27	J/mol×K	561.65	NIST
Cp,gas	90.46	J/mol×K	603.25	NIST
Cp,liquid	[68.44; 74.48]	J/mol×K	[94.00; 200.00]
Cp,liquid	68.50	J/mol×K	94.00	NIST
Cp,liquid	68.66	J/mol×K	100.00	NIST
Cp,liquid	68.44	J/mol×K	100.32	NIST
Cp,liquid	72.22	J/mol×K	180.00	NIST
Cp,liquid	74.48	J/mol×K	200.00	NIST
ΔfusH	[0.58; 2.86]	kJ/mol	[89.50; 90.34]
ΔfusH	2.79	kJ/mol	89.50	NIST
ΔfusH	2.79	kJ/mol	89.50	NIST
ΔfusH	2.86	kJ/mol	89.90	NIST
ΔfusH	0.58	kJ/mol	90.30	NIST
ΔfusH	0.58	kJ/mol	90.34	NIST
ΔsubH	[20.50; 22.60]	kJ/mol	[85.00; 90.00]
ΔsubH	22.60	kJ/mol	85.00	NIST
ΔsubH	20.50	kJ/mol	90.00	NIST
ΔvapH	[13.26; 17.70]	kJ/mol	[112.00; 289.00]
ΔvapH	17.70	kJ/mol	112.00	NIST
ΔvapH	17.10	kJ/mol	117.50	NIST
ΔvapH	15.30	kJ/mol	168.00	NIST
ΔvapH	15.70	kJ/mol	169.50	NIST
ΔvapH	14.70	kJ/mol	184.00	NIST
ΔvapH	14.70	kJ/mol	184.10	NIST
ΔvapH	14.71	kJ/mol	184.60	KDB
ΔvapH	14.49	kJ/mol	191.67	Enthalpy of Vaporization Measurements of Liquid Methane, Ethane, and Methane + Ethane by Differential Scanning Calorimetry at Low Temperatures and High Pressures
ΔvapH	14.90	kJ/mol	207.00	NIST
ΔvapH	13.89	kJ/mol	208.94	Enthalpy of Vaporization Measurements of Liquid Methane, Ethane, and Methane + Ethane by Differential Scanning Calorimetry at Low Temperatures and High Pressures
ΔvapH	14.70	kJ/mol	210.00	NIST
ΔvapH	13.26	kJ/mol	213.47	Enthalpy of Vaporization Measurements of Liquid Methane, Ethane, and Methane + Ethane by Differential Scanning Calorimetry at Low Temperatures and High Pressures
ΔvapH	14.90	kJ/mol	251.00	NIST
ΔvapH	15.30	kJ/mol	289.00	NIST
Pvap	[53.57; 4806.00]	kPa	[173.63; 304.65]
Pvap	53.57	kPa	173.63	Vapor-liquid and vapor-liquid-liquid equilibrium measurements and correlation of the binary mixtures 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) p (tetrafluoromethane (R14), trifluoromethane (R23), octafluoropropane (R218), nitrogen (R728) and argon (R740)) and ethane (R170) p trifluoromethane (R23)
Pvap	66.42	kPa	177.24	Vapor-liquid and vapor-liquid-liquid equilibrium measurements and correlation of the binary mixtures 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) p (tetrafluoromethane (R14), trifluoromethane (R23), octafluoropropane (R218), nitrogen (R728) and argon (R740)) and ethane (R170) p trifluoromethane (R23)
Pvap	77.00	kPa	179.68	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
Pvap	88.97	kPa	182.33	Vapour pressure and excess Gibbs free energy of binary mixtures of hydrogen sulphide with ethane, propane, and n-butane at temperature of 182.33 K
Pvap	94.31	kPa	183.28	Vapor-liquid and vapor-liquid-liquid equilibrium measurements and correlation of the binary mixtures 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) p (tetrafluoromethane (R14), trifluoromethane (R23), octafluoropropane (R218), nitrogen (R728) and argon (R740)) and ethane (R170) p trifluoromethane (R23)
Pvap	123.80	kPa	188.31	Vapor-Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
Pvap	136.00	kPa	190.14	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
Pvap	159.00	kPa	193.28	Vapor-Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
Pvap	204.70	kPa	198.66	Vapor-Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
Pvap	223.00	kPa	200.68	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
Pvap	336.00	kPa	210.03	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
Pvap	374.30	kPa	212.84	Vapor-Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
Pvap	665.40	kPa	228.50	Vapor-Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
Pvap	673.93	kPa	228.82	Vapor-liquid and vapor-liquid-liquid equilibrium measurements and correlation of the binary mixtures 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) p (tetrafluoromethane (R14), trifluoromethane (R23), octafluoropropane (R218), nitrogen (R728) and argon (R740)) and ethane (R170) p trifluoromethane (R23)
Pvap	1084.00	kPa	243.76	Vapor-Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
Pvap	1862.00	kPa	264.05	Isothermal Vapor Liquid Equilibrium Data and Modeling for the Ethane (R170) + Perfluoropropane (R218) System at Temperatures from (264 to 308) K
Pvap	2275.00	kPa	271.05	Isothermal Vapor Liquid Equilibrium Data and Modeling for the Ethane (R170) + Perfluoropropane (R218) System at Temperatures from (264 to 308) K
Pvap	2700.00	kPa	278.05	Isothermal Vapor Liquid Equilibrium Data and Modeling for the Ethane (R170) + Perfluoropropane (R218) System at Temperatures from (264 to 308) K
Pvap	2699.00	kPa	278.15	Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
Pvap	2793.00	kPa	279.82	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	2970.00	kPa	282.49	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	3155.00	kPa	285.10	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	3324.00	kPa	287.43	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	3542.00	kPa	290.31	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	3735.00	kPa	292.81	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	4003.00	kPa	296.02	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	4154.00	kPa	297.72	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	4379.00	kPa	300.21	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	4560.00	kPa	302.13	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Pvap	4600.00	kPa	303.04	Isothermal Vapor Liquid Equilibrium Data and Modeling for the Ethane (R170) + Perfluoropropane (R218) System at Temperatures from (264 to 308) K
Pvap	4806.00	kPa	304.65	Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
ρl	548.00	kg/m3	183.00	KDB
ΔfusS	6.46	J/mol×K	90.34	NIST
γ	0.02	N/m	153.20	KDB
ΔvapS	79.87	J/mol×K	184.10	NIST

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (2)
3. Mass density, kg/m3 (1)
4. Mass density, kg/m3 (2)
5. Speed of sound, m/s (2)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
108.15	1050.00	67.90
108.15	2020.00	67.87
108.15	4290.00	67.78
118.15	1060.00	68.26
118.15	2030.00	67.63
118.15	4290.00	68.95
128.15	4310.00	68.65
143.15	4080.00	68.62
153.15	4070.00	69.94
163.15	4050.00	70.84
188.15	1120.00	73.46
188.15	4310.00	72.41
228.15	1170.00	81.04
228.15	4320.00	80.07
238.15	1210.00	83.71
238.15	4330.00	82.72
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Viscosity, Pa*s - Gas
290.00	79.60	8.9940e-06
290.00	103.08	8.9980e-06
290.00	124.24	9.0010e-06
290.00	148.27	9.0060e-06
290.00	176.98	9.0090e-06
290.00	202.62	9.0130e-06
290.00	225.58	9.0130e-06
290.00	246.46	9.0150e-06
290.00	271.01	9.0180e-06
290.00	300.59	9.0190e-06
290.00	327.37	9.0230e-06
290.00	353.88	9.0260e-06
290.00	378.73	9.0290e-06
290.00	412.83	9.0320e-06
290.00	437.94	9.0370e-06
290.00	476.96	9.0420e-06
290.00	508.87	9.0480e-06
290.00	556.20	9.0530e-06
290.00	595.19	9.0590e-06
290.00	636.89	9.0630e-06
290.00	671.53	9.0680e-06
290.00	710.98	9.0750e-06
290.00	775.23	9.0840e-06
290.00	825.27	9.0950e-06
290.00	882.03	9.1030e-06
290.00	913.28	9.1090e-06
290.00	958.42	9.1200e-06
290.00	1009.50	9.1310e-06
290.00	1064.40	9.1420e-06
290.00	1123.30	9.1550e-06
290.00	1181.70	9.1690e-06
290.00	1216.60	9.1770e-06
290.00	1259.30	9.1880e-06
290.00	1350.10	9.2130e-06
290.00	1438.10	9.2390e-06
290.00	1484.80	9.2500e-06
290.00	1559.50	9.2750e-06
290.00	1615.30	9.2930e-06
290.00	1667.30	9.3080e-06
290.00	1716.80	9.3260e-06
290.00	1816.00	9.3650e-06
290.00	1884.50	9.3910e-06
290.00	1946.80	9.4160e-06
290.00	2026.70	9.4510e-06
290.00	2080.60	9.4750e-06
290.00	2139.40	9.5020e-06
290.00	2227.50	9.5470e-06
290.00	2279.90	9.5740e-06
290.00	2347.30	9.6110e-06
290.00	2438.70	9.6640e-06
290.00	2475.40	9.6900e-06
290.00	2532.70	9.7250e-06
290.00	2602.60	9.7730e-06
290.00	2675.10	9.8220e-06
290.00	2747.80	9.8790e-06
290.00	2795.40	9.9180e-06
290.00	2853.60	9.9680e-06
290.00	2890.10	0.0000
290.00	2916.00	0.0000
300.00	71.39	9.3010e-06
300.00	102.60	9.3040e-06
300.00	125.56	9.3100e-06
300.00	151.72	9.3120e-06
300.00	178.40	9.3120e-06
300.00	203.62	9.3150e-06
300.00	224.20	9.3230e-06
300.00	254.24	9.3230e-06
300.00	275.46	9.3240e-06
300.00	305.63	9.3290e-06
300.00	334.53	9.3330e-06
300.00	358.06	9.3370e-06
300.00	388.48	9.3400e-06
300.00	419.92	9.3440e-06
300.00	447.23	9.3480e-06
300.00	481.95	9.3520e-06
300.00	507.29	9.3550e-06
300.00	545.78	9.3620e-06
300.00	579.91	9.3650e-06
300.00	618.84	9.3720e-06
300.00	649.95	9.3770e-06
300.00	683.78	9.3810e-06
300.00	728.32	9.3870e-06
300.00	778.72	9.3960e-06
300.00	813.14	9.4050e-06
300.00	869.08	9.4130e-06
300.00	911.25	9.4200e-06
300.00	974.32	9.4340e-06
300.00	1013.50	9.4440e-06
300.00	1064.60	9.4540e-06
300.00	1116.40	9.4640e-06
300.00	1160.00	9.4740e-06
300.00	1251.50	9.4960e-06
300.00	1321.30	9.5160e-06
300.00	1364.60	9.5250e-06
300.00	1446.40	9.5480e-06
300.00	1514.90	9.5680e-06
300.00	1551.00	9.5800e-06
300.00	1610.70	9.5990e-06
300.00	1653.60	9.6110e-06
300.00	1760.90	9.6460e-06
300.00	1829.20	9.6720e-06
300.00	1871.30	9.6880e-06
300.00	1910.30	9.6990e-06
300.00	2005.60	9.7380e-06
300.00	2082.70	9.7710e-06
300.00	2130.40	9.7910e-06
300.00	2244.00	9.8430e-06
300.00	2333.80	9.8840e-06
300.00	2391.70	9.9140e-06
300.00	2455.40	9.9470e-06
300.00	2558.40	0.0000
300.00	2606.20	0.0000
300.00	2688.10	0.0000
300.00	2745.70	0.0000
300.00	2853.70	0.0000
300.00	2904.90	0.0000
300.00	2986.60	0.0000
300.00	3054.50	0.0000
300.00	3131.80	0.0000
300.00	3213.80	0.0000
300.00	3267.40	0.0000
300.00	3349.10	0.0000
300.00	3404.20	0.0000
300.00	3483.60	0.0000
300.00	3535.20	0.0000
300.00	3619.90	0.0000
300.00	3692.70	0.0000
300.00	3760.00	0.0000
300.00	3800.70	0.0000
300.00	3838.00	0.0000
310.00	100.00	9.6000e-06
310.00	123.15	9.6050e-06
310.00	148.48	9.6070e-06
310.00	175.41	9.6090e-06
310.00	200.44	9.6170e-06
310.00	226.30	9.6200e-06
310.00	248.76	9.6210e-06
310.00	274.29	9.6240e-06
310.00	299.70	9.6290e-06
310.00	328.47	9.6310e-06
310.00	354.89	9.6350e-06
310.00	382.87	9.6350e-06
310.00	439.93	9.6450e-06
310.00	468.57	9.6480e-06
310.00	498.24	9.6540e-06
310.00	533.99	9.6590e-06
310.00	581.86	9.6660e-06
310.00	623.38	9.6750e-06
310.00	670.29	9.6780e-06
310.00	714.00	9.6860e-06
310.00	756.22	9.6940e-06
310.00	815.85	9.7060e-06
310.00	859.52	9.7110e-06
310.00	924.11	9.7260e-06
310.00	983.07	9.7380e-06
310.00	1052.80	9.7520e-06
310.00	1133.60	9.7700e-06
310.00	1191.40	9.7850e-06
310.00	1251.40	9.7980e-06
310.00	1357.60	9.8240e-06
310.00	1428.80	9.8430e-06
310.00	1497.20	9.8620e-06
310.00	1568.90	9.8840e-06
310.00	1607.50	9.8950e-06
310.00	1714.10	9.9280e-06
310.00	1790.80	9.9520e-06
310.00	1833.70	9.9670e-06
310.00	1917.40	9.9960e-06
310.00	1998.30	0.0000
310.00	2078.30	0.0000
310.00	2158.00	0.0000
310.00	2236.30	0.0000
310.00	2348.30	0.0000
310.00	2449.30	0.0000
310.00	2529.40	0.0000
310.00	2633.40	0.0000
310.00	2741.50	0.0000
310.00	2846.90	0.0000
310.00	2926.80	0.0000
310.00	3015.60	0.0000
310.00	3161.00	0.0000
310.00	3229.90	0.0000
310.00	3346.20	0.0000
310.00	3445.60	0.0000
310.00	3573.20	0.0000
310.00	3666.30	0.0000
310.00	3799.10	0.0000
310.00	3907.90	0.0000
310.00	4097.00	0.0000
310.00	4223.40	0.0000
310.00	4370.50	0.0000
310.00	4494.90	0.0000
310.00	4596.30	0.0000
310.00	4702.60	0.0000
310.00	4809.20	0.0000
310.00	4892.20	0.0000
310.00	4941.20	0.0000
310.00	5009.40	0.0000
310.00	5055.90	0.0000
310.00	5108.70	0.0000
310.00	5164.00	0.0000
310.00	5195.50	0.0000
310.00	5222.40	0.0000
310.00	5255.50	0.0000
310.00	5272.20	0.0000
310.00	5296.90	0.0000
310.00	5317.40	0.0000
310.00	5335.70	0.0000
310.00	5354.20	0.0000
310.00	5374.80	0.0000
310.00	5394.80	0.0000
310.00	5414.00	0.0000
310.00	5435.10	0.0000
310.00	5460.20	0.0000
310.00	5493.20	0.0000
310.00	5530.60	0.0000
310.00	5581.20	0.0000
310.00	5645.50	0.0000
310.00	5736.20	0.0000
310.00	5848.80	0.0000
310.00	5991.90	0.0000
310.00	6166.70	0.0000
310.00	6385.60	0.0000
310.00	6844.20	0.0000
310.00	7383.20	0.0000
310.00	8208.10	0.0000
310.00	8880.40	0.0000
310.00	9706.30	0.0000
310.00	10618.00	0.0000
310.00	11697.00	0.0000
310.00	12756.00	0.0001
310.00	14805.00	0.0001
310.00	16313.00	0.0001
310.00	18248.00	0.0001
310.00	19609.00	0.0001
310.00	22390.00	0.0001
310.00	24935.00	0.0001
320.00	119.57	9.8990e-06
320.00	152.92	9.9040e-06
320.00	181.50	9.9100e-06
320.00	215.30	9.9140e-06
320.00	243.93	9.9180e-06
320.00	278.70	9.9230e-06
320.00	313.02	9.9270e-06
320.00	345.57	9.9320e-06
320.00	377.95	9.9330e-06
320.00	412.10	9.9390e-06
320.00	448.82	9.9430e-06
320.00	477.80	9.9510e-06
320.00	509.18	9.9550e-06
320.00	544.11	9.9610e-06
320.00	584.95	9.9620e-06
320.00	620.20	9.9730e-06
320.00	670.29	9.9790e-06
320.00	719.06	9.9840e-06
320.00	781.87	9.9950e-06
320.00	854.01	0.0000
320.00	899.65	0.0000
320.00	952.26	0.0000
320.00	1049.80	0.0000
320.00	1125.90	0.0000
320.00	1222.50	0.0000
320.00	1345.60	0.0000
320.00	1449.60	0.0000
320.00	1525.60	0.0000
320.00	1639.00	0.0000
320.00	1757.00	0.0000
320.00	1853.70	0.0000
320.00	1962.10	0.0000
320.00	2068.20	0.0000
320.00	2212.00	0.0000
320.00	2327.40	0.0000
320.00	2466.70	0.0000
320.00	2594.20	0.0000
320.00	2710.60	0.0000
320.00	2850.10	0.0000
320.00	2965.50	0.0000
320.00	3083.10	0.0000
320.00	3226.80	0.0000
320.00	3372.10	0.0000
320.00	3495.10	0.0000
320.00	3628.00	0.0000
320.00	3711.20	0.0000
320.00	3995.50	0.0000
320.00	4174.20	0.0000
320.00	4326.40	0.0000
320.00	4506.50	0.0000
320.00	4679.80	0.0000
320.00	4802.60	0.0000
320.00	4971.50	0.0000
320.00	5150.20	0.0000
320.00	5276.00	0.0000
320.00	5401.10	0.0000
320.00	5516.40	0.0000
320.00	5655.90	0.0000
320.00	5738.60	0.0000
320.00	5847.90	0.0000
320.00	5934.60	0.0000
320.00	6017.40	0.0000
320.00	6083.40	0.0000
320.00	6131.80	0.0000
320.00	6201.30	0.0000
320.00	6270.10	0.0000
320.00	6344.60	0.0000
320.00	6421.50	0.0000
320.00	6484.30	0.0000
320.00	6542.40	0.0000
320.00	6603.20	0.0000
320.00	6699.90	0.0000
320.00	6820.60	0.0000
320.00	6970.00	0.0000
320.00	7084.60	0.0000
320.00	7278.40	0.0000
320.00	7560.50	0.0000
320.00	7921.50	0.0000
320.00	8226.40	0.0000
320.00	8606.90	0.0000
320.00	9057.30	0.0000
320.00	9550.80	0.0000
320.00	10191.00	0.0000
320.00	10925.00	0.0000
320.00	12245.00	0.0000
320.00	13361.00	0.0000
320.00	15697.00	0.0001
320.00	17376.00	0.0001
320.00	19353.00	0.0001
320.00	21685.00	0.0001
320.00	24197.00	0.0001
320.00	25347.00	0.0001
340.00	105.61	0.0000
340.00	135.53	0.0000
340.00	173.00	0.0000
340.00	203.75	0.0000
340.00	246.71	0.0000
340.00	281.07	0.0000
340.00	317.73	0.0000
340.00	340.53	0.0000
340.00	365.44	0.0000
340.00	406.17	0.0000
340.00	430.83	0.0000
340.00	471.02	0.0000
340.00	524.00	0.0000
340.00	563.09	0.0000
340.00	632.12	0.0000
340.00	668.44	0.0000
340.00	746.01	0.0000
340.00	826.84	0.0000
340.00	865.72	0.0000
340.00	924.23	0.0000
340.00	978.06	0.0000
340.00	1047.10	0.0000
340.00	1133.50	0.0000
340.00	1206.60	0.0000
340.00	1333.70	0.0000
340.00	1452.90	0.0000
340.00	1550.00	0.0000
340.00	1616.00	0.0000
340.00	1729.50	0.0000
340.00	1841.80	0.0000
340.00	1956.30	0.0000
340.00	2076.00	0.0000
340.00	2208.90	0.0000
340.00	2348.80	0.0000
340.00	2499.00	0.0000
340.00	2602.70	0.0000
340.00	2711.90	0.0000
340.00	2892.80	0.0000
340.00	3009.10	0.0000
340.00	3131.30	0.0000
340.00	3257.10	0.0000
340.00	3452.10	0.0000
340.00	3564.40	0.0000
340.00	3674.20	0.0000
340.00	3778.40	0.0000
340.00	3876.00	0.0000
340.00	3952.90	0.0000
340.00	4079.40	0.0000
340.00	4236.70	0.0000
340.00	4399.00	0.0000
340.00	4487.20	0.0000
340.00	4577.50	0.0000
340.00	4669.50	0.0000
340.00	4964.90	0.0000
340.00	5080.40	0.0000
340.00	5188.40	0.0000
340.00	5312.30	0.0000
340.00	5429.80	0.0000
340.00	5556.80	0.0000
340.00	6232.10	0.0000
340.00	6448.50	0.0000
340.00	6663.50	0.0000
340.00	6848.40	0.0000
340.00	7040.90	0.0000
340.00	7221.80	0.0000
340.00	7403.80	0.0000
340.00	7583.40	0.0000
340.00	8081.60	0.0000
340.00	8262.80	0.0000
340.00	8448.50	0.0000
340.00	8644.60	0.0000
340.00	8861.90	0.0000
340.00	9077.10	0.0000
340.00	9322.70	0.0000
340.00	9574.50	0.0000
340.00	9854.70	0.0000
340.00	10697.00	0.0000
340.00	11140.00	0.0000
340.00	11651.00	0.0000
340.00	12243.00	0.0000
340.00	12873.00	0.0000
340.00	13585.00	0.0000
340.00	14512.00	0.0000
340.00	15608.00	0.0000
340.00	16887.00	0.0000
340.00	18734.00	0.0000
340.00	20544.00	0.0000
340.00	22692.00	0.0001
340.00	24738.00	0.0001
370.00	113.32	0.0000
370.00	147.46	0.0000
370.00	180.32	0.0000
370.00	219.78	0.0000
370.00	250.53	0.0000
370.00	277.77	0.0000
370.00	320.51	0.0000
370.00	346.69	0.0000
370.00	373.36	0.0000
370.00	400.72	0.0000
370.00	439.73	0.0000
370.00	485.60	0.0000
370.00	519.47	0.0000
370.00	562.25	0.0000
370.00	598.82	0.0000
370.00	639.50	0.0000
370.00	742.62	0.0000
370.00	790.53	0.0000
370.00	851.13	0.0000
370.00	897.21	0.0000
370.00	957.22	0.0000
370.00	1061.30	0.0000
370.00	1145.10	0.0000
370.00	1245.00	0.0000
370.00	1356.80	0.0000
370.00	1444.20	0.0000
370.00	1544.00	0.0000
370.00	1691.60	0.0000
370.00	1792.10	0.0000
370.00	1890.40	0.0000
370.00	2039.80	0.0000
370.00	2203.90	0.0000
370.00	2348.70	0.0000
370.00	2474.50	0.0000
370.00	2660.20	0.0000
370.00	2735.40	0.0000
370.00	2950.00	0.0000
370.00	3097.60	0.0000
370.00	3253.80	0.0000
370.00	3413.10	0.0000
370.00	3571.80	0.0000
370.00	3749.70	0.0000
370.00	4010.60	0.0000
370.00	4256.80	0.0000
370.00	4408.20	0.0000
370.00	4642.80	0.0000
370.00	4829.10	0.0000
370.00	5031.80	0.0000
370.00	5303.70	0.0000
370.00	5567.20	0.0000
370.00	5790.40	0.0000
370.00	5962.10	0.0000
370.00	6228.20	0.0000
370.00	6502.90	0.0000
370.00	6800.20	0.0000
370.00	7065.00	0.0000
370.00	7360.20	0.0000
370.00	7672.90	0.0000
370.00	8020.10	0.0000
370.00	8250.40	0.0000
370.00	8589.30	0.0000
370.00	8848.50	0.0000
370.00	9106.30	0.0000
370.00	9463.40	0.0000
370.00	9764.30	0.0000
370.00	10125.00	0.0000
370.00	10524.00	0.0000
370.00	10821.00	0.0000
370.00	11121.00	0.0000
370.00	11584.00	0.0000
370.00	11948.00	0.0000
370.00	12311.00	0.0000
370.00	12696.00	0.0000
370.00	13112.00	0.0000
370.00	14179.00	0.0000
370.00	14733.00	0.0000
370.00	15324.00	0.0000
370.00	15969.00	0.0000
370.00	17164.00	0.0000
370.00	18821.00	0.0000
370.00	20693.00	0.0000
370.00	23709.00	0.0000
370.00	25448.00	0.0000
370.00	27478.00	0.0000
370.00	29959.00	0.0000
400.00	113.97	0.0000
400.00	143.04	0.0000
400.00	172.06	0.0000
400.00	220.10	0.0000
400.00	256.28	0.0000
400.00	290.91	0.0000
400.00	313.22	0.0000
400.00	340.31	0.0000
400.00	379.05	0.0000
400.00	412.95	0.0000
400.00	452.22	0.0000
400.00	493.06	0.0000
400.00	539.15	0.0000
400.00	583.20	0.0000
400.00	612.60	0.0000
400.00	650.91	0.0000
400.00	697.00	0.0000
400.00	769.42	0.0000
400.00	828.12	0.0000
400.00	882.81	0.0000
400.00	935.77	0.0000
400.00	1048.20	0.0000
400.00	1174.60	0.0000
400.00	1279.30	0.0000
400.00	1386.00	0.0000
400.00	1491.30	0.0000
400.00	1572.90	0.0000
400.00	1673.50	0.0000
400.00	1797.20	0.0000
400.00	1896.50	0.0000
400.00	2054.70	0.0000
400.00	2240.00	0.0000
400.00	2392.10	0.0000
400.00	2533.00	0.0000
400.00	2674.50	0.0000
400.00	2841.80	0.0000
400.00	3003.50	0.0000
400.00	3194.50	0.0000
400.00	3340.90	0.0000
400.00	3516.80	0.0000
400.00	3669.80	0.0000
400.00	3778.40	0.0000
400.00	3988.00	0.0000
400.00	4168.40	0.0000
400.00	4352.60	0.0000
400.00	4582.40	0.0000
400.00	4783.40	0.0000
400.00	4973.10	0.0000
400.00	5178.50	0.0000
400.00	5404.20	0.0000
400.00	5646.70	0.0000
400.00	5902.20	0.0000
400.00	6167.00	0.0000
400.00	6465.30	0.0000
400.00	6870.00	0.0000
400.00	7332.70	0.0000
400.00	7767.60	0.0000
400.00	8216.20	0.0000
400.00	8682.80	0.0000
400.00	9060.00	0.0000
400.00	9435.60	0.0000
400.00	9837.10	0.0000
400.00	10232.00	0.0000
400.00	10615.00	0.0000
400.00	11009.00	0.0000
400.00	11425.00	0.0000
400.00	11864.00	0.0000
400.00	12272.00	0.0000
400.00	12725.00	0.0000
400.00	13189.00	0.0000
400.00	14034.00	0.0000
400.00	14540.00	0.0000
400.00	15072.00	0.0000
400.00	15650.00	0.0000
400.00	16442.00	0.0000
400.00	17258.00	0.0000
400.00	18095.00	0.0000
400.00	18892.00	0.0000
400.00	19765.00	0.0000
400.00	20714.00	0.0000
400.00	21765.00	0.0000
400.00	22931.00	0.0000
400.00	24246.00	0.0000
400.00	25689.00	0.0000
400.00	27359.00	0.0000
400.00	29228.00	0.0000
430.00	138.54	0.0000
430.00	186.79	0.0000
430.00	220.94	0.0000
430.00	248.21	0.0000
430.00	284.70	0.0000
430.00	314.45	0.0000
430.00	338.20	0.0000
430.00	360.36	0.0000
430.00	400.10	0.0000
430.00	429.22	0.0000
430.00	460.50	0.0000
430.00	521.75	0.0000
430.00	572.47	0.0000
430.00	607.44	0.0000
430.00	670.06	0.0000
430.00	737.74	0.0000
430.00	783.92	0.0000
430.00	862.64	0.0000
430.00	905.70	0.0000
430.00	976.56	0.0000
430.00	1087.40	0.0000
430.00	1180.90	0.0000
430.00	1348.40	0.0000
430.00	1446.40	0.0000
430.00	1530.80	0.0000
430.00	1620.80	0.0000
430.00	1717.10	0.0000
430.00	1818.00	0.0000
430.00	1924.70	0.0000
430.00	2096.80	0.0000
430.00	2291.40	0.0000
430.00	2428.10	0.0000
430.00	2573.50	0.0000
430.00	2724.20	0.0000
430.00	2898.60	0.0000
430.00	3053.20	0.0000
430.00	3194.60	0.0000
430.00	3356.60	0.0000
430.00	3507.90	0.0000
430.00	3656.90	0.0000
430.00	3831.30	0.0000
430.00	3954.50	0.0000
430.00	4110.60	0.0000
430.00	4343.80	0.0000
430.00	4492.10	0.0000
430.00	4786.00	0.0000
430.00	5105.40	0.0000
430.00	5477.70	0.0000
430.00	5739.30	0.0000
430.00	6014.30	0.0000
430.00	6310.10	0.0000
430.00	6613.30	0.0000
430.00	6932.10	0.0000
430.00	7322.60	0.0000
430.00	7787.20	0.0000
430.00	8292.40	0.0000
430.00	8671.00	0.0000
430.00	9056.80	0.0000
430.00	9598.50	0.0000
430.00	10163.00	0.0000
430.00	10894.00	0.0000
430.00	11360.00	0.0000
430.00	11839.00	0.0000
430.00	12362.00	0.0000
430.00	12882.00	0.0000
430.00	13394.00	0.0000
430.00	14177.00	0.0000
430.00	14772.00	0.0000
430.00	15400.00	0.0000
430.00	16025.00	0.0000
430.00	16743.00	0.0000
430.00	17527.00	0.0000
430.00	18351.00	0.0000
430.00	19231.00	0.0000
430.00	20081.00	0.0000
430.00	21171.00	0.0000
430.00	22413.00	0.0000
430.00	23636.00	0.0000
430.00	24931.00	0.0000
430.00	26291.00	0.0000
430.00	27712.00	0.0000
430.00	29313.00	0.0000
430.00	30906.00	0.0000
Reference

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	64.37	9.0750e-06
293.15	80.37	9.0760e-06
293.15	80.42	9.0750e-06
293.15	80.48	9.0730e-06
293.15	160.10	9.0820e-06
293.15	160.16	9.0820e-06
293.15	315.97	9.1020e-06
293.15	316.05	9.0990e-06
293.15	467.91	9.1180e-06
293.15	467.96	9.1190e-06
293.15	468.01	9.1180e-06
293.15	615.93	9.1390e-06
293.15	616.03	9.1370e-06
293.15	759.69	9.1620e-06
293.15	889.73	9.1830e-06
293.15	889.87	9.1830e-06
293.15	1036.20	9.2120e-06
293.15	1036.30	9.2130e-06
293.15	1167.20	9.2460e-06
293.15	1167.30	9.2430e-06
293.15	1293.60	9.2740e-06
293.15	1293.80	9.2750e-06
293.15	1420.80	9.3050e-06
293.15	1421.00	9.3100e-06
293.15	1992.40	9.5060e-06
293.15	1992.50	9.5060e-06
293.15	1992.60	9.5050e-06
293.15	2477.20	9.7490e-06
293.15	2477.40	9.7480e-06
293.15	2477.60	9.7480e-06
293.15	2879.70	0.0000
293.15	2879.90	0.0000
293.15	3212.10	0.0000
293.15	3212.20	0.0000
293.15	3212.30	0.0000
293.15	3471.90	0.0000
293.15	3472.00	0.0000
293.15	3472.20	0.0000
293.15	3577.60	0.0000
293.15	3577.80	0.0000
293.15	64.37	9.0740e-06
293.15	160.10	9.0830e-06
293.15	316.05	9.0980e-06
293.15	615.93	9.1370e-06
293.15	759.69	9.1650e-06
293.15	889.73	9.1840e-06
293.15	1036.20	9.2130e-06
293.15	1167.30	9.2430e-06
293.15	1293.80	9.2750e-06
293.15	1420.80	9.3080e-06
293.15	759.69	9.1620e-06
307.15	92.55	9.4920e-06
307.15	92.62	9.4890e-06
307.15	160.18	9.5080e-06
307.15	332.45	9.5430e-06
307.15	493.91	9.5730e-06
307.15	493.97	9.5720e-06
307.15	649.95	9.6040e-06
307.15	650.01	9.6040e-06
307.15	800.35	9.6350e-06
307.15	800.41	9.6360e-06
307.15	959.13	9.6750e-06
307.15	959.20	9.6740e-06
307.15	1094.40	9.7090e-06
307.15	1094.50	9.7100e-06
307.15	1233.80	9.7460e-06
307.15	1233.90	9.7460e-06
307.15	1343.40	9.7780e-06
307.15	1502.40	9.8280e-06
307.15	2134.40	0.0000
307.15	2134.50	0.0000
307.15	2674.20	0.0000
307.15	2674.30	0.0000
307.15	3138.10	0.0000
307.15	3138.20	0.0000
307.15	3138.40	0.0000
307.15	3539.60	0.0000
307.15	3539.80	0.0000
307.15	3889.00	0.0000
307.15	3892.40	0.0000
307.15	4150.50	0.0000
307.15	4151.60	0.0000
307.15	4152.00	0.0000
307.15	4152.40	0.0000
307.15	4328.60	0.0000
307.15	4329.50	0.0000
307.15	4330.10	0.0000
307.15	4330.40	0.0000
307.15	4331.50	0.0000
307.15	4514.60	0.0000
307.15	4516.20	0.0000
307.15	4517.40	0.0000
307.15	4518.30	0.0000
307.15	4519.20	0.0000
307.15	4736.30	0.0000
307.15	4736.70	0.0000
307.15	4939.20	0.0000
307.15	4939.30	0.0000
307.15	5019.40	0.0000
307.15	5019.50	0.0000
307.15	5042.90	0.0000
307.15	5043.00	0.0000
307.15	5051.00	0.0000
307.15	5051.10	0.0000
307.15	5058.70	0.0000
307.15	5058.80	0.0000
307.15	5060.30	0.0000
307.15	5060.40	0.0000
307.15	5064.10	0.0000
307.15	5064.20	0.0000
307.15	5105.00	0.0000
307.15	5105.10	0.0000
307.15	5105.20	0.0000
307.15	5160.60	0.0000
307.15	5160.90	0.0000
307.15	5161.00	0.0000
307.15	5348.10	0.0000
307.15	5348.30	0.0000
307.15	5348.50	0.0000
307.15	5348.60	0.0000
307.15	5648.10	0.0000
307.15	5648.30	0.0000
307.15	5648.70	0.0000
307.15	5648.80	0.0000
307.15	6326.20	0.0000
307.15	6328.20	0.0000
307.15	6328.50	0.0000
307.15	6328.90	0.0000
307.15	7598.20	0.0000
307.15	7602.20	0.0000
307.15	7603.00	0.0000
307.15	9627.40	0.0000
307.15	9628.10	0.0000
307.15	12507.00	0.0001
307.15	12508.00	0.0001
307.15	12509.00	0.0001
307.15	15941.00	0.0001
307.15	15981.00	0.0001
307.15	15985.00	0.0001
307.15	15986.00	0.0001
307.15	15987.00	0.0001
307.15	160.18	9.5100e-06
307.15	332.45	9.5420e-06
307.15	800.41	9.6390e-06
307.15	959.20	9.6740e-06
307.15	1343.40	9.7780e-06
307.15	1502.40	9.8300e-06
307.15	2674.20	0.0000
307.15	2674.30	0.0000
307.15	4939.30	0.0000
307.15	5019.40	0.0000
307.15	5043.00	0.0000
307.15	5051.00	0.0000
307.15	5051.10	0.0000
307.15	5058.70	0.0000
307.15	5058.80	0.0000
307.15	5060.30	0.0000
307.15	5064.10	0.0000
307.15	5064.20	0.0000
307.15	5105.00	0.0000
307.15	5161.00	0.0000
307.15	5058.80	0.0000
307.15	5064.10	0.0000
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Mass density, kg/m3 - Gas
265.07	1811.51	32.6652
265.08	1612.28	27.8016
265.08	1404.49	23.2391
265.10	1199.36	19.1462
265.10	1004.37	15.548
265.10	816.83	12.3046
265.02	505.80	7.3166
265.06	279.98	3.9405
265.06	116.65	1.6114
259.63	1548.63	27.5129
259.63	1351.60	23.0046
259.63	1351.53	23.0156
259.62	1174.87	19.3302
259.62	933.39	14.7341
259.63	726.92	11.1161
259.63	550.88	8.2159
259.63	358.50	5.211
259.63	152.52	2.1615
254.74	1474.67	26.843
254.76	1280.41	22.2529
254.76	1280.46	22.2533
254.76	1040.10	17.2189
254.76	825.19	13.1528
254.76	634.94	9.817
254.77	423.98	6.354
254.73	225.89	3.2988
254.72	114.93	1.6547
249.80	1281.64	23.1579
249.81	1281.26	23.1411
249.81	1067.47	18.3574
249.81	1067.48	18.3577
249.79	863.82	14.2661
249.80	863.80	14.2677
249.81	633.60	10.0488
249.81	360.58	5.4802
249.82	147.60	2.1773
244.95	1111.38	20.0202
244.93	904.97	15.5558
244.91	1111.57	20.0182
244.91	880.77	15.0548
244.92	877.28	14.9812
244.92	628.26	10.2258
244.93	350.79	5.4481
244.93	350.80	5.4496
244.93	138.73	2.0893
240.01	954.18	17.1448
239.99	717.05	12.2167
240.04	502.79	8.2138
240.04	323.60	5.1239
240.04	105.82	1.619
235.03	694.56	12.1431
235.01	592.34	10.1286
235.01	499.46	8.3818
235.00	391.54	6.4356
235.01	305.16	4.9382
235.02	197.50	3.137
230.36	615.49	10.8842
230.35	493.22	8.4852
230.35	391.01	6.5852
230.34	306.85	5.0853
230.35	197.35	3.2054
225.47	499.44	8.8558
225.44	403.34	6.9981
225.41	310.68	5.2843
225.42	212.66	3.5454
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
469.94	10882.00	98.22
399.00	10202.00	130.49
469.95	21121.00	194.69
469.96	31179.00	260.81
399.00	20736.00	270.05
469.98	41149.00	303.71
399.01	30973.00	330.57
469.97	55719.00	346.04
399.00	42071.00	368.25
304.30	10173.00	372.8
469.97	70405.00	376.04
399.00	55861.00	399.66
469.97	86507.00	401.16
304.30	20724.00	417.38
399.00	69356.00	422.4
469.96	105448.00	424.56
470.00	120161.00	439.65
304.30	30964.00	441.74
469.99	125610.00	444.69
399.00	86735.00	444.78
469.97	137417.00	454.98
304.30	41974.00	460.6
399.00	103351.00	462.05
399.02	120965.00	477.5
399.01	123093.00	479.22
304.29	56004.00	479.29
399.01	136122.00	489.14
304.30	69715.00	494.0
304.30	86990.00	509.02
304.30	103841.00	521.63
304.30	113927.00	528.42
304.31	120907.00	532.8
304.30	137643.00	542.63
Reference

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
298.15	2000.00	29.226
298.15	5987.00	352.999
298.15	7909.00	371.593
298.15	10071.00	385.867
298.15	14959.00	407.911
298.15	20004.00	423.934
298.15	24927.00	436.235
298.15	29893.00	446.599
298.15	35020.00	455.82
298.15	39905.00	463.582
298.15	49977.00	477.362
298.15	75091.00	503.592
298.15	99827.00	523.125
298.15	119760.00	536.225
298.15	149807.00	552.995
350.00	1999.00	22.819
350.00	29974.00	384.889
350.00	49928.00	430.315
350.00	74959.00	464.696
350.00	100019.00	489.111
350.00	124863.00	508.192
350.00	149906.00	524.195
350.00	172157.00	536.528
400.00	805.00	7.452
400.00	7325.00	84.481
400.00	27286.00	311.921
400.00	48575.00	383.533
400.00	69346.00	421.214
400.00	92289.00	450.02
400.00	117459.00	473.901
400.00	139686.00	491.026
400.00	154657.00	501.119
400.00	166558.00	508.474
400.00	181565.00	517.111
400.00	196062.00	524.823
450.00	1998.00	16.685
450.00	5021.00	44.467
450.00	10001.00	96.599
450.00	20005.00	202.282
450.00	30018.00	272.417
450.00	49974.00	346.238
450.00	69967.00	388.105
450.00	79928.00	403.693
450.00	99962.00	429.113
450.00	119860.00	449.29
450.00	139478.00	465.963
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
240.00	4105.93	925.763
240.00	5106.52	940.945
240.00	6107.17	955.52
240.00	7107.81	969.562
240.00	8108.48	983.126
240.00	9109.14	996.249
240.00	10109.80	1008.96
240.00	10110.00	1008.98
240.00	12611.70	1039.17
240.00	15113.30	1067.42
240.00	17615.00	1094.0
240.00	20116.60	1119.17
240.00	25119.90	1165.94
240.00	30123.10	1208.8
240.00	35126.40	1248.52
240.00	40130.30	1285.64
240.00	45133.50	1320.54
240.00	50136.80	1353.53
240.00	60143.40	1414.76
240.00	70149.90	1470.8
240.00	80157.40	1522.63
240.00	90164.10	1571.0
240.00	100171.00	1616.41
260.00	4105.20	758.383
260.00	4105.21	758.386
260.00	5105.87	779.502
260.00	6106.58	799.28
260.00	7107.27	817.917
260.00	8107.95	835.581
260.00	9108.59	852.394
260.00	10109.20	868.453
260.00	10108.80	868.423
260.00	25118.20	1054.69
260.00	30121.60	1103.09
260.00	35125.00	1147.34
260.00	40129.20	1188.26
260.00	45132.60	1226.43
260.00	50136.10	1262.28
260.00	60142.90	1328.26
260.00	60142.90	1328.25
260.00	70149.80	1388.14
280.01	4105.15	566.583
280.01	5105.80	601.029
280.01	6106.50	631.087
280.01	7107.21	657.999
280.01	8107.89	682.515
280.00	9108.55	705.137
280.01	10109.20	726.207
280.01	12610.90	773.631
280.01	15112.60	815.405
280.01	17614.40	853.035
280.01	20116.10	887.449
280.01	25119.50	948.992
280.01	30122.90	1003.29
280.01	35126.30	1052.22
280.01	40129.70	1096.96
280.01	45132.90	1138.35
280.01	50136.20	1176.96
280.01	60142.90	1247.48
280.00	70149.60	1311.0
280.00	80156.30	1369.01
280.00	90163.00	1422.61
280.00	100169.00	1472.55
300.00	5104.86	368.772
300.00	6105.63	434.335
300.00	7106.43	481.551
300.00	8107.14	519.902
300.00	9107.82	552.801
300.00	10108.50	581.928
300.00	12610.20	643.77
300.00	15111.90	695.353
300.00	17613.30	740.223
300.00	20115.10	780.276
300.00	25118.60	850.196
300.00	30122.00	910.523
300.00	35125.50	964.074
300.00	40128.90	1012.53
300.00	45132.60	1056.98
300.00	50135.90	1098.18
300.00	60142.80	1172.9
300.00	70149.50	1239.68
300.00	80156.30	1300.36
300.00	90163.10	1356.21
300.00	100170.00	1408.09
305.32	6104.96	370.713
305.32	7105.78	429.663
305.32	8106.55	474.293
305.32	9107.32	511.282
305.32	10108.00	543.313
305.32	12609.80	609.924
305.32	15111.60	664.48
305.32	17613.40	711.441
305.32	20115.20	753.077
305.32	25118.70	825.252
305.32	25119.00	825.252
305.32	30122.20	887.154
305.32	35125.40	941.89
305.32	40129.00	991.286
305.32	45132.30	1036.51
305.32	50135.70	1078.35
305.32	60142.40	1154.11
305.32	70148.90	1221.7
305.32	80155.40	1283.04
305.32	90161.80	1339.44
305.32	100168.00	1391.79
Reference

Operational condition: Frequency, MHz = 0.005 (Gas)

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Speed of sound, m/s - Gas
280.01	500.43	294.645
280.01	500.43	294.646
280.01	500.43	294.645
280.02	500.43	294.647
280.02	500.44	294.647
280.02	500.43	294.648
319.55	463.50	316.216
319.55	463.51	316.218
319.95	464.08	316.403
319.95	464.09	316.405
324.99	479.74	318.642
324.99	479.75	318.646
325.00	479.75	318.647
325.00	479.75	318.649
325.00	479.75	318.649
325.00	479.76	318.65
339.37	492.93	325.401
339.37	492.93	325.401
339.89	493.66	325.638
339.89	493.66	325.639
359.27	522.10	334.296
359.27	522.11	334.297
359.85	523.03	334.572
359.85	523.03	334.572
365.00	479.42	337.342
365.00	479.42	337.344
365.01	479.42	337.345
365.01	479.42	337.345
365.01	479.43	337.344
365.01	479.42	337.346
365.01	479.42	337.346
365.01	479.42	337.347
365.01	479.43	337.348
379.19	551.11	342.951
379.19	551.11	342.953
379.76	551.90	343.188
379.77	551.90	343.189
399.22	579.97	351.407
399.22	579.97	351.409
399.80	580.93	351.687
399.80	580.93	351.688
404.98	531.39	354.225
404.98	531.41	354.222
404.98	531.41	354.222
404.98	531.39	354.225
404.98	531.40	354.226
404.98	531.40	354.226
404.98	531.40	354.226
404.98	531.41	354.222
404.98	531.40	354.227
419.45	608.87	359.755
419.46	608.88	359.757
419.91	609.51	359.943
419.92	609.52	359.946
444.98	496.45	370.717
444.98	496.45	370.719
444.98	496.45	370.719
444.98	496.44	370.716
444.98	496.45	370.716
444.98	496.45	370.718
444.98	496.45	370.719
444.99	496.45	370.717
444.99	496.45	370.719
484.95	497.53	386.13
484.95	497.54	386.131
484.95	497.55	386.141
484.95	497.55	386.142
484.95	497.52	386.129
484.95	497.56	386.144
484.96	539.52	386.002
484.96	497.55	386.136
484.96	497.55	386.137
484.96	497.55	386.138
484.96	539.51	386.0
484.96	539.52	386.002
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
η	[0.0028599; 0.0001360]	Pa×s	[92.72; 213.75]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.12365e+01
Coefficient B			4.98760e+02
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			92.72
Temperature range, max.			213.75
η	0.0028599	Pa×s	92.72	Calculated Property
η	0.0014467	Pa×s	106.16	Calculated Property
η	0.0008531	Pa×s	119.61	Calculated Property
η	0.0005597	Pa×s	133.06	Calculated Property
η	0.0003967	Pa×s	146.51	Calculated Property
η	0.0002980	Pa×s	159.96	Calculated Property
η	0.0002340	Pa×s	173.41	Calculated Property
η	0.0001902	Pa×s	186.86	Calculated Property
η	0.0001590	Pa×s	200.31	Calculated Property
η	0.0001360	Pa×s	213.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4860.82]	kPa	[130.32; 305.32]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39922e+01
Coefficient B			-1.60935e+03
Coefficient C			-1.28860e+01
Temperature range, min.			130.32
Temperature range, max.			305.32
Pvap	1.33	kPa	130.32	Calculated Property
Pvap	9.34	kPa	149.76	Calculated Property
Pvap	40.34	kPa	169.21	Calculated Property
Pvap	125.98	kPa	188.65	Calculated Property
Pvap	313.61	kPa	208.10	Calculated Property
Pvap	661.77	kPa	227.54	Calculated Property
Pvap	1233.55	kPa	246.99	Calculated Property
Pvap	2089.89	kPa	266.43	Calculated Property
Pvap	3284.52	kPa	285.88	Calculated Property
Pvap	4860.82	kPa	305.32	Calculated Property
Pvap	[1.13e-03; 4883.10]	kPa	[90.35; 305.42]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			4.63913e+01
Coefficient B			-2.62673e+03
Coefficient C			-5.38156e+00
Coefficient D			1.60186e-05
Coefficient E			0.00000e+00
Temperature range, min.			90.35
Temperature range, max.			305.42
Pvap	1.13e-03	kPa	90.35	Calculated Property
Pvap	0.15	kPa	114.25	Calculated Property
Pvap	3.19	kPa	138.14	Calculated Property
Pvap	25.05	kPa	162.04	Calculated Property
Pvap	109.65	kPa	185.94	Calculated Property
Pvap	332.59	kPa	209.83	Calculated Property
Pvap	793.26	kPa	233.73	Calculated Property
Pvap	1608.09	kPa	257.63	Calculated Property
Pvap	2913.99	kPa	281.52	Calculated Property
Pvap	4883.10	kPa	305.42	Calculated Property
Pvap	[1.54e-03; 5.77]	kPa	[91.33; 144.13]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49831e+01
Coefficient B			-1.82204e+03
Coefficient C			-6.42200e+00
Reference			Carruth and Kobayashi, 1973
Temperature range, min.			91.33
Temperature range, max.			144.13
Pvap	1.54e-03	kPa	91.33	Calculated Property
Pvap	6.16e-03	kPa	97.20	Calculated Property
Pvap	0.02	kPa	103.06	Calculated Property
Pvap	0.06	kPa	108.93	Calculated Property
Pvap	0.16	kPa	114.80	Calculated Property
Pvap	0.38	kPa	120.66	Calculated Property
Pvap	0.83	kPa	126.53	Calculated Property
Pvap	1.68	kPa	132.40	Calculated Property
Pvap	3.20	kPa	138.26	Calculated Property
Pvap	5.77	kPa	144.13	Calculated Property
Pvap	[2.48; 217.26]	kPa	[135.74; 199.91]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36736e+01
Coefficient B			-1.51911e+03
Coefficient C			-1.67190e+01
Reference			Loomis and Walters, 1926
Temperature range, min.			135.74
Temperature range, max.			199.91
Pvap	2.48	kPa	135.74	Calculated Property
Pvap	5.11	kPa	142.87	Calculated Property
Pvap	9.74	kPa	150.00	Calculated Property
Pvap	17.37	kPa	157.13	Calculated Property
Pvap	29.29	kPa	164.26	Calculated Property
Pvap	47.09	kPa	171.39	Calculated Property
Pvap	72.59	kPa	178.52	Calculated Property
Pvap	107.89	kPa	185.65	Calculated Property
Pvap	155.29	kPa	192.78	Calculated Property
Pvap	217.26	kPa	199.91	Calculated Property

Similar Compounds

Find more compounds similar to Ethane.

Mixtures

• Ethane + Hydrogen sulfide
• Ethane + 1-Butanol
• 2-PROPANOL, 1,1,1,3,3,3-HEXAFLUORO- + Ethane + Water
• Methane + Ethane
• Ethane + Methane, trifluoro-
• Furan, tetrahydro-2,5-dimethyl- + Ethane + Furan, tetrahydro-2,5-dimethyl-, cis-
• 2-Propanol + Ethane
• Nitrogen + Ethane
• Methane + Ethane + Pentane
• Ethane + Methyl Alcohol
• Carbon dioxide + Ethane
• Nitrogen + Methane + Ethane
• Ammonia + Ethane
• 1,2-Ethanediol + Ethane
• Ethane, hexafluoro- + Ethane
• Ethane + Decanoic acid, methyl ester
• Ethane + Dodecanoic acid, methyl ester
• Ethane + Methyl tetradecanoate
• Ethane + Hexadecanoic acid, methyl ester
• Ethane + Methyl stearate

Find more mixtures with Ethane.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Thermal Conductivity of Mixtures of Carbon Dioxide and Ethane in the Critical Region
• The Experimental Study of Temperature Dependence of Binary Diffusion Coefficients of Gases at Different Pressures
• Measurement and modeling of hydrocarbon dew points for five synthetic natural gas mixtures
• Low-pressure solubilities and thermodynamics of solvation of eight gases in 1-butyl-3-methylimidazolium hexafluorophosphate
• Vapor liquid equilibrium measurements and correlations for an azeotropic system of ethane + hexafluoroethane
• Vapor liquid equilibrium in the system ethane + ethylene glycol
• Solubility of carbon dioxide and ethane in three ionic liquids based on the bis{(trifluoromethyl)sulfonyl}imide anion
• Vapor-liquid and liquid-liquid equilibrium properties of ethane + methanol system at ambient temperature
• Phase behaviour of high molecular mass methyl esters in supercritical ethane
• Solubilities of several non-polar gases in mixtures water + 2,2,2-trifluoroethanol at 298.15 K and 101.33 kPa
• Surface tension of an ethane-nitrogen solution. 1: Experiment and thermodynamic analysis of the results
• Isothermal vapor-liquid equilibrium of R170 + n-perfluorooctane at 308 - 338 K: Measurement, equation of state modelling, and molecular simulation
• Surface tension of ethane-methane solutions: 1. Experiment and thermodynamic analysis of the results
• High pressure phase equilibria of binary mixtures of light hydrocarbons in the ionic liquid 1-hexyl-3-methylimidazoliumtetracyanoborate
• Effects of association with impurities in ammonia purification
• Measurements of the speed of sound in liquid and supercritical ethane
• Anomalous nucleation near a fluid phase boundary created by a rapid heat pulse
• Vapor-liquid and vapor-liquid-liquid equilibrium measurements and correlation of the binary mixtures 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) p (tetrafluoromethane (R14), trifluoromethane (R23), octafluoropropane (R218), nitrogen (R728) and argon (R740)) and ethane (R170) p trifluoromethane (R23)
• Effect of cation on the solubility of ethane in three bis(fluorosulfonyl)imide ([FSI]) based low viscosity ionic liquids
• Experimental P(rho)T-x measurements of liquid methane-ethane-nitrogen mixtures
• Solubility of carbon dioxide, ethane, methane, oxygen, nitrogen, hydrogen, argon, and carbon monoxide in 1-butyl-3-methylimidazolium tetrafluoroborate between temperatures 283 K and 343 K and at pressures close to atmospheric
• Vapour pressure and excess Gibbs free energy of binary mixtures of hydrogen sulphide with ethane, propane, and n-butane at temperature of 182.33 K
• (Vapor + liquid) equilibrium properties of (ethane + ethanol) system at (295, 303, and 313) K
• Solubility of carbon dioxide, nitrous oxide, ethane, and nitrogen in 1-butyl-1-methylpyrrolidinium and trihexyl(tetradecyl)phosphonium tris(pentafluoroethyl)trifluorophosphate (eFAP) ionic liquids
• Solubility of gases in 1-alkyl-3methylimidazolium alkyl sulfate ionic liquids: Experimental determination and modeling
• Experimental and modeling investigations of solubility and saturated liquid densities and viscosities for binary systems (methane +, ethane +, and carbon dioxide + 2-propanol)
• Solubility of carbon dioxide, methane, and ethane in 1-butanol and saturated liquid densities and viscosities
• Apparatus based on a compact single-sinker densimeter and measurements of the (p,.rho.,T) relation of difluoromethane
• Spherical resonator for vapor-phase speed of sound and measurements of 1,1,1,2,2,3,3-heptafluoro-3-methoxypropane (RE347mcc) and trans-1,3,3,3-tetrafluoropropene [R1234ze(E)]
• Surface tension and critical point measurements of methane + propane mixtures
• Vapour-phase (p,rho,T,x) behaviour and virial coefficients for the (ethane + carbon dioxide) system
• Solubility of gases in fluoroorganic alcohols. Part III. Solubilities of several non-polar gases in water + 1,1,1,3,3,3-hexafluoropropan-2-ol at 298.15 K and 101.33 kPa
• Solubilities of gases in cycloethers. The solubility of 13 nonpolar gases in 2,5-dimethyltetrahydrofuran at 273.15 to 303.15 K and 101.32 kPa
• Measurement and Calculation of CO2 Frost Points in CH4 + CO2/CH4 + CO2 + N2/CH4 + CO2 + C2H6 Mixtures at Low Temperatures
• Reference Quality Vapor-Liquid Equilibrium Data for the Binary Systems Methane + Ethane, + Propane, + Butane and, + 2-Methylpropane, at Temperatures from (203 to 273) K and Pressures to 9 MPa
• Accurate p-.rho.-T Data for a Synthetic Residual Natural Gas Mixture (0.95 CH4 + 0.04 C2H6 + 0.01 C3H8) at Temperatures between (135 and 500) K at Pressures to 200 MPa
• Density Measurements for Ethane, Carbon Dioxide, and Methane + Nitrogen Mixtures from 300 to 470 K up to 137 MPa Using a Vibrating Tube Densimeter
• Enthalpy of Vaporization Measurements of Liquid Methane, Ethane, and Methane + Ethane by Differential Scanning Calorimetry at Low Temperatures and High Pressures
• Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
• Isothermal Vapor-Liquid Equilibrium Measurements for the (R1234ze(E) + Ethane) System at Temperatures from 272.27 to 347.52 K
• Measurement and Prediction of Hydrocarbon Dew Points of Synthetic Natural Gas Mixtures
• Bubble Point Measurements of Neopentane + Ethane Mixtures
• Fluid Phase Equilibria of Binary n-Alkane + Squalane Systems
• Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
• Measurement of the Water Solubility in the Gas Phase of the Ethane + Water Binary System near Hydrate Forming Conditions
• Solubility of Ethane in N-Formyl Morpholine
• Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
• P-rho-T and VLE for Ethane + Hydrogen Sulfide from (254.05 to 363.21) K at Pressures up to 20 MPa
• Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
• Solubility of Ethane in Diethylene Glycol
• Vapor-Liquid Equilibrium Measurements for the Ethane + Hexafluoroethane System over a Temperature Range from (199.64 to 242.93) K
• Viscosity Measurements on Gaseous Ethane
• Isochoric PVTx measurements for the C2H6 + N2O binary system
• Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
• Solubility of Ethane in Aqueous Solutions of Monoethanolamine and Diethanolamine
• Vapor-Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
• Experimental Determination and Correlation of Phase Equilibria for the Ethane + 1-Propanol and Propane + 1-Propanol Systems
• Measurement of Carbon Dioxide Freezing in Mixtures of Methane, Ethane, and Nitrogen in the Solid-Vapor Equilibrium Region
• Low-Pressure Solubility and Thermodynamics of Solvation of Carbon Dioxide, Ethane, and Hydrogen in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide between Temperatures of 283 K and 343 K
• Accurate P-rho-T Data and Phase Boundary Determination for a Synthetic Residual Natural Gas Mixture
• High-Pressure Multiphase Behavior of the Ternary Systems (Ethene + Water + Acetone) and (Ethane + Water + Acetone)
• Solubility of Ethane in Aqueous Solutions of 2-(2-Aminoethoxy)ethanol
• Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
• Simultaneous Viscosity-Density Measurements on Ethane and Propane over a Wide Range of Temperature and Pressure Including the Near-Critical Region
• Equilibrium Phase Densities, Interfacial Tensions for the Ethane + n-Pentane System at 294.15 K
• Equilibrium Phase Densities, Vapor Phase Compositions, and Interfacial Tensions for the Methane + Ethane + n-Pentane System at 294.15 K
• Measurement and Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n-Tetradecane) Binary Systems
• Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
• Determination of CO2 Solubility in Saturated Liquid CH4 + N2 and CH4 + C2H6 Mixtures above Atmospheric Pressure
• Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
• Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
• Vapor Liquid Equilibrium for the Mixture Methane (CH4) + Ethane (C2H6) over the Temperature Range (126.01 to 140.01) K
• Isothermal Vapor Liquid Equilibrium Data and Modeling for the Ethane (R170) + Perfluoropropane (R218) System at Temperatures from (264 to 308) K
• New Vapor Liquid Liquid Equilibrium Data for Ethane and Propane in Alkanolamine Aqueous Solutions
• Measuring and Modeling the Solubility and Density for CO2 Toluene and C2H6 Toluene Systems
• Vapor-Liquid Equilibria and Saturated Liquid Densities in Binary Mixtures of Nitrogen, Methane, and Ethane and Their Correlation Using the VTPR and PSRK GCEOS
• High-Pressure Phase Behavior of Ethane with 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide
• Solubilities of Carbon Dioxide, Methane, and Ethane in Sodium Chloride Solution Containing Gas Hydrate
• Accurate PVT Data for Ethane from (298 to 450) K up to 200 MPa
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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