Chemical Properties of Propene, hexafluoro- (CAS 116-15-4)

InChI

InChI=1S/C3F6/c4-1(2(5)6)3(7,8)9

InChI Key

HCDGVLDPFQMKDK-UHFFFAOYSA-N

Formula

C3F6

SMILES

FC(F)=C(F)C(F)(F)F

Molecular Weight¹

150.02

CAS

116-15-4

Other Names

• 1,1,2,3,3,3-hexafluoro-1-propene
• 1-Propene, 1,1,2,3,3,3-hexafluoro-
• CF3CF=CF2
• HFC 1216
• Hexafluoro-1-propene
• Propylene, hexafluoro-
• UN 1858
• hexafluoropropene
• hexafluoropropylene
• perfluoro-1-propene
• perfluoropropene
• perfluoropropylene

• C_p,gas : Ideal gas heat capacity (J/mol×K).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• 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
ΔfH°gas	-1151.70	kJ/mol	NIST
ΔfusH°	12.17	kJ/mol	Joback Calculated Property
IE	[10.30; 11.11]	eV
IE	10.60 ± 0.03	eV	NIST
IE	10.60 ± 0.03	eV	NIST
IE	10.62	eV	NIST
IE	10.62	eV	NIST
IE	11.11	eV	NIST
IE	10.30 ± 0.20	eV	NIST
logPoct/wat	2.626		Crippen Calculated Property
McVol	59.450	ml/mol	McGowan Calculated Property
Inp	[268.00; 268.00]
Inp	268.00		NIST
Inp	268.00		NIST
Tboil	[244.00; 244.20]	K
Tboil	244.00	K	NIST
Tboil	244.20	K	NIST
Tboil	244.00 ± 3.00	K	NIST

Cheméo can also estimate Normal melting (fusion) point, Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[100.76; 131.83]	J/mol×K	[264.35; 395.75]
Cp,gas	100.76	J/mol×K	264.35	Joback Calculated Property
Cp,gas	106.72	J/mol×K	286.25	Joback Calculated Property
Cp,gas	112.36	J/mol×K	308.15	Joback Calculated Property
Cp,gas	117.67	J/mol×K	330.05	Joback Calculated Property
Cp,gas	122.68	J/mol×K	351.95	Joback Calculated Property
Cp,gas	127.39	J/mol×K	373.85	Joback Calculated Property
Cp,gas	131.83	J/mol×K	395.75	Joback Calculated Property
ΔvapH	21.90	kJ/mol	263.00	NIST
Pvap	[64.00; 3128.10]	kPa	[233.17; 358.76]
Pvap	64.00	kPa	233.17	Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap	102.00	kPa	243.23	Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap	120.00	kPa	248.14	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	157.00	kPa	253.14	Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap	149.70	kPa	253.26	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	150.00	kPa	253.27	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	184.10	kPa	258.26	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	225.00	kPa	263.01	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	224.50	kPa	263.16	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	224.50	kPa	263.17	Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
Pvap	233.00	kPa	263.20	Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap	278.57	kPa	268.13	Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Pvap	272.00	kPa	268.24	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	327.10	kPa	272.33	Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Pvap	324.40	kPa	273.16	Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
Pvap	334.00	kPa	273.19	Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap	326.80	kPa	273.24	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	394.08	kPa	278.14	Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Pvap	392.00	kPa	278.20	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	389.00	kPa	278.21	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	388.60	kPa	278.22	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	420.70	kPa	279.64	Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Pvap	452.00	kPa	282.92	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	459.00	kPa	283.23	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	542.58	kPa	288.14	Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Pvap	537.10	kPa	288.21	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	538.00	kPa	288.22	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	617.00	kPa	292.76	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	641.00	kPa	293.12	Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
Pvap	625.90	kPa	293.19	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	641.00	kPa	293.96	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	670.00	kPa	295.42	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	721.00	kPa	297.93	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	729.82	kPa	298.14	Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Pvap	728.30	kPa	298.22	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	763.30	kPa	299.34	Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Pvap	774.00	kPa	300.38	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	825.70	kPa	302.24	Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Pvap	838.00	kPa	302.94	Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
Pvap	832.00	kPa	303.07	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	834.00	kPa	303.08	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	839.70	kPa	303.22	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	890.00	kPa	305.40	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	953.00	kPa	307.90	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	963.24	kPa	308.19	Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Pvap	963.40	kPa	308.21	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	1018.00	kPa	310.38	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	1077.30	kPa	312.33	Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Pvap	1087.00	kPa	312.90	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	1094.00	kPa	312.91	Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
Pvap	1099.40	kPa	313.11	Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
Pvap	1099.90	kPa	313.21	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	1099.00	kPa	313.38	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	1159.00	kPa	315.32	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	1232.10	kPa	317.63	Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Pvap	1235.00	kPa	317.82	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	1250.60	kPa	318.22	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	1251.16	kPa	318.22	Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Pvap	1315.00	kPa	320.30	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	1398.00	kPa	322.79	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	1407.00	kPa	322.94	Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
Pvap	1408.00	kPa	323.06	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	1413.50	kPa	323.20	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	1488.00	kPa	325.34	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	1579.00	kPa	327.86	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	1595.10	kPa	328.21	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	1676.00	kPa	330.38	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	1776.00	kPa	332.85	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	1783.00	kPa	332.94	Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
Pvap	1788.20	kPa	333.11	Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
Pvap	1791.40	kPa	333.21	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	1863.00	kPa	334.96	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	1879.00	kPa	335.31	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	1993.00	kPa	337.90	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	2007.90	kPa	338.18	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	2110.00	kPa	340.34	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	2230.00	kPa	342.86	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	2225.00	kPa	342.92	Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
Pvap	2243.80	kPa	343.21	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	2345.00	kPa	345.26	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	2486.00	kPa	347.82	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	2500.50	kPa	348.22	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	2757.00	kPa	352.78	Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Pvap	2778.20	kPa	353.14	Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
Pvap	2782.30	kPa	353.23	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	2903.00	kPa	355.24	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	2965.30	kPa	356.24	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	2998.50	kPa	356.76	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	3017.50	kPa	357.06	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	3031.00	kPa	357.27	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	3044.20	kPa	357.47	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	3050.40	kPa	357.56	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	3095.10	kPa	358.26	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
Pvap	3128.10	kPa	358.76	Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene

Datasets

1. Mass density, kg/m3 (1)
2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	2000.00	1326.6
Reference

Speed of sound, m/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
1130.00	273.17	488.3
1150.00	253.27	575.6
1160.00	288.15	424.2
1990.00	303.15	370.7
2300.00	323.18	288.3
4760.00	343.19	245.5
5200.00	288.15	468.9
8270.00	343.19	311.3
10090.00	303.15	463.9
10130.00	288.15	513.8
10400.00	273.17	567.9
10440.00	343.19	341.8
10450.00	363.15	287.0
10550.00	323.18	404.9
10940.00	253.27	645.3
15690.00	383.16	310.6
16670.00	403.14	288.3
19600.00	423.15	293.5
25040.00	273.17	660.8
25100.00	423.15	345.1
25130.00	448.15	318.1
25160.00	303.15	576.7
25160.00	473.14	298.7
25190.00	288.15	618.0
25500.00	363.15	442.0
25610.00	403.14	375.7
25690.00	383.16	407.4
25910.00	253.27	728.8
28790.00	323.18	547.0
50080.00	288.15	741.2
50150.00	273.17	779.5
50380.00	323.18	664.6
50460.00	473.14	462.3
50520.00	363.15	592.9
50530.00	383.16	562.3
50540.00	343.19	627.2
50710.00	448.15	485.0
50800.00	423.15	513.0
50890.00	403.14	537.5
50920.00	303.15	709.3
52820.00	253.27	844.3
75030.00	253.27	921.1
75240.00	448.15	596.6
75280.00	273.17	871.7
75340.00	323.18	767.2
75370.00	303.15	804.5
75400.00	423.15	623.9
75440.00	288.15	837.6
75490.00	363.15	700.6
75570.00	473.14	576.7
75610.00	343.19	730.9
75640.00	403.14	647.4
75940.00	383.16	673.9
100060.00	403.14	737.1
100170.00	288.15	916.1
100220.00	473.14	666.6
100230.00	273.17	949.0
100300.00	363.15	787.2
100500.00	383.16	761.1
100560.00	303.15	886.5
100630.00	253.27	997.3
100650.00	343.19	818.3
100710.00	423.15	715.4
100750.00	448.15	689.4
101090.00	323.18	852.8
125070.00	323.18	921.8
125170.00	343.19	890.4
125230.00	363.15	861.9
125320.00	423.15	791.3
125410.00	303.15	956.2
125430.00	273.17	1017.1
125510.00	288.15	986.4
125570.00	473.14	745.3
125630.00	383.16	837.2
125630.00	403.14	813.6
125710.00	448.15	766.5
125810.00	253.27	1063.0
150160.00	423.15	858.8
150270.00	273.17	1077.5
150340.00	343.19	956.2
150340.00	363.15	928.6
150360.00	403.14	880.3
150460.00	383.16	903.4
150630.00	288.15	1048.4
150670.00	323.18	987.4
150690.00	473.14	814.0
150770.00	448.15	834.5
150900.00	303.15	1020.1
151420.00	253.27	1123.6
174830.00	253.27	1174.3
175160.00	343.19	1014.7
175250.00	288.15	1103.9
175320.00	448.15	894.5
175340.00	303.15	1075.6
175410.00	423.15	920.3
175590.00	363.15	988.8
175620.00	403.14	941.6
175680.00	323.18	1045.2
175720.00	473.14	875.3
175770.00	383.16	964.4
175810.00	273.17	1133.8
200290.00	343.19	1069.0
200320.00	363.15	1042.8
200450.00	253.27	1224.7
200520.00	423.15	976.3
200670.00	403.14	997.2
200700.00	273.17	1184.6
200700.00	288.15	1156.6
200740.00	383.16	1019.4
200750.00	323.18	1098.6
200800.00	473.14	931.7
200820.00	448.15	951.6
200830.00	303.15	1129.0
250190.00	303.15	1221.9
250220.00	343.19	1165.9
250260.00	383.16	1116.8
250380.00	288.15	1249.0
250420.00	423.15	1075.9
250500.00	403.14	1096.0
250580.00	253.27	1315.5
250600.00	473.14	1031.5
250610.00	363.15	1141.2
250620.00	323.18	1193.8
250800.00	273.17	1276.7
250910.00	448.15	1051.8
299650.00	253.27	1393.8
300040.00	288.15	1331.1
300360.00	363.15	1226.7
300390.00	423.15	1163.6
300400.00	323.18	1278.0
300450.00	273.17	1358.2
300620.00	343.19	1252.0
300640.00	473.14	1119.7
300660.00	403.14	1183.8
300690.00	383.16	1204.6
300750.00	303.15	1306.5
300780.00	448.15	1139.3
350100.00	343.19	1327.9
350190.00	253.27	1468.5
350280.00	383.16	1282.6
350300.00	303.15	1381.1
350560.00	473.14	1199.0
350600.00	423.15	1243.0
350610.00	403.14	1262.3
350690.00	363.15	1305.3
350710.00	448.15	1218.3
350810.00	323.18	1355.4
350820.00	273.17	1432.3
350970.00	288.15	1407.7
400020.00	303.15	1450.2
400090.00	273.17	1499.6
400260.00	363.15	1376.0
400280.00	403.14	1333.6
400370.00	343.19	1399.8
400410.00	288.15	1475.2
400510.00	383.16	1354.3
400580.00	323.18	1424.9
400740.00	253.27	1535.4
400750.00	473.14	1272.0
400820.00	448.15	1291.1
400920.00	423.15	1315.6
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[173.19; 263.52]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.37505e+01
Coefficient B			-2.04277e+03
Coefficient C			-2.14600e+01
Temperature range, min.			173.19
Temperature range, max.			263.52
Pvap	1.33	kPa	173.19	Calculated Property
Pvap	3.07	kPa	183.23	Calculated Property
Pvap	6.43	kPa	193.26	Calculated Property
Pvap	12.39	kPa	203.30	Calculated Property
Pvap	22.29	kPa	213.34	Calculated Property
Pvap	37.84	kPa	223.37	Calculated Property
Pvap	61.10	kPa	233.41	Calculated Property
Pvap	94.47	kPa	243.45	Calculated Property
Pvap	140.66	kPa	253.48	Calculated Property
Pvap	202.63	kPa	263.52	Calculated Property
Pvap	[4.07e-04; 2809.65]	kPa	[116.65; 368.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			3.44036e+01
Coefficient B			-3.28864e+03
Coefficient C			-2.94220e+00
Coefficient D			-1.05992e-06
Temperature range, min.			116.65
Temperature range, max.			368.00
Pvap	4.07e-04	kPa	116.65	Calculated Property
Pvap	0.05	kPa	144.58	Calculated Property
Pvap	1.17	kPa	172.51	Calculated Property
Pvap	10.57	kPa	200.43	Calculated Property
Pvap	52.90	kPa	228.36	Calculated Property
Pvap	178.38	kPa	256.29	Calculated Property
Pvap	456.90	kPa	284.22	Calculated Property
Pvap	959.39	kPa	312.14	Calculated Property
Pvap	1737.31	kPa	340.07	Calculated Property
Pvap	2809.65	kPa	368.00	Calculated Property

Similar Compounds

Find more compounds similar to Propene, hexafluoro-.

Mixtures

• Propene + Propene, hexafluoro-
• Propene, hexafluoro- + Ethylene
• Carbon dioxide + Propene, hexafluoro-
• Propane + Propene, hexafluoro-
• Butane + Propene, hexafluoro-
• 1-Butene + Propene, hexafluoro-
• Propene, hexafluoro- + Cyclobutane, octafluoro-
• Ethane + Propene, hexafluoro-
• Propene, hexafluoro- + Cyclohexane, methyl-
• Propene, hexafluoro- + Cyclohexane
• n-Hexane + Propene, hexafluoro-
• Propene, hexafluoro- + 2,2,3,3,4,4,4-Heptafluoro-butanol
• Propene, hexafluoro- + Furan, tetrahydro-2-methyl-
• Ethene, tetrafluoro- + Propene, hexafluoro-
• Ethane, hexafluoro- + Propene, hexafluoro-
• Toluene + Propene, hexafluoro-
• Propene, hexafluoro- + Ethane, 2,2-dichloro-1,1,1-trifluoro-
• Propene, hexafluoro- + Hexafluoropropylene oxide

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
• Crippen Method
• Crippen Method
• Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
• Phase equilibrium data for mixtures involving 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane between 312 and 343 K
• Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
• Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
• Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
• Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
• Vapor-Liquid Equilibrium Data for Binary Systems Consisting of Either Hexafluoropropene (HFP) or 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane (HFPO) with Carbon Dioxide (R-744) or 2,2-Dichloro-1,1,1-trifluoroethane (R-123)
• Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
• Speeds of Sound in Liquid and Supercritical Hexafluoropropylene (HFP) and Hexafluoropropylene Oxide (HFPO) at Pressures up to 400 MPa
• Liquid-Phase p-rho-T Data for 2,3,3,3-Tetrafluoroprop-1-ene (R-1234yf) and 1,1,2,3,3,3-Hexafluoroprop-1-ene (R-1216) at Temperatures from (208 to 353) K under Pressures up to 40 MPa
• Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
• Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
• Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,3,3,3-Hexafluoroprop-1-ene +1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (292 to 352) K and Pressures up to 2.6 MPa
• Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
• Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
• Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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