Chemical Properties of Tetrafluoromethane (CAS 75-73-0)

InChI

InChI=1S/CF4/c2-1(3,4)5

InChI Key

TXEYQDLBPFQVAA-UHFFFAOYSA-N

Formula

CF4

SMILES

FC(F)(F)F

Molecular Weight¹

88.00

CAS

75-73-0

Other Names

• Arcton 0
• CF4
• CFC 14
• Carbon fluoride
• Carbon fluoride (CF4)
• F 14
• FC 14
• Freon 14
• Halocarbon 14
• Halon 14
• Methane, tetrafluo-
• Methane, tetrafluoro-
• R 14
• R 14 (Refrigerant)
• R-14
• Refrigerant 14
• Refrigerant R 14
• Tetrafluoromethane [R14]
• UN 1982
• carbon tetrafluoride
• perfluoromethane

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid 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).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• 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_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).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• I_np : Non-polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.1760		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
PAff	529.30	kJ/mol	NIST
BasG	503.70	kJ/mol	NIST
ΔcH°liquid	[-2222.30; -1519.89]	kJ/mol
ΔcH°liquid	-1519.89	kJ/mol	NIST
ΔcH°liquid	-2222.30	kJ/mol	NIST
εr	1.00		NCMS SOLV-DB
ΔfG°	-818.86	kJ/mol	Joback Calculated Property
ΔfH°gas	[-953.40; -678.00]	kJ/mol
ΔfH°gas	-933.38 ± 0.27	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-933.00	kJ/mol	NIST
ΔfH°gas	-933.20 ± 0.80	kJ/mol	NIST
ΔfH°gas	-933.20 ± 0.75	kJ/mol	NIST
ΔfH°gas	-953.40 ± 1.60	kJ/mol	NIST
ΔfH°gas	-934.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-920.90 ± 5.90	kJ/mol	NIST
ΔfH°gas	-917.10 ± 9.60	kJ/mol	NIST
ΔfH°gas	-908.80 ± 5.00	kJ/mol	NIST
ΔfH°gas	-913.40	kJ/mol	NIST
ΔfH°gas	-922.20	kJ/mol	NIST
ΔfH°gas	-912.00 ± 8.00	kJ/mol	NIST
ΔfH°gas	Outlier -678.00 ± 8.00	kJ/mol	NIST
ΔfusH°	3.25	kJ/mol	Joback Calculated Property
ΔvapH°	11.67	kJ/mol	NCMS SOLV-DB
IE	[14.70; 16.50]	eV
IE	14.70	eV	NIST
IE	16.20 ± 0.10	eV	NIST
IE	15.30	eV	NIST
IE	16.20	eV	NIST
IE	14.70	eV	NIST
IE	16.50	eV	NIST
IE	15.70	eV	NIST
IE	16.20	eV	NIST
IE	16.26	eV	NIST
IE	16.25 ± 0.04	eV	NIST
IE	16.20	eV	NIST
log10WS	-0.09		Relay (1.0) Calculated Property
logPoct/wat	1.180		NCMS SOLV-DB
McVol	32.030	ml/mol	McGowan Calculated Property
Pc	[3680.00; 3745.00]	kPa
Pc	3680.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	3738.89	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3745.00 ± 10.00	kPa	NIST
Ptriple	0.11 ± 0.00	kPa	Staveley, Lobo and Calado (1981), triple points Compiled value
ρc	629.67 ± 0.88	kg/m3	NIST
Inp	82.00		NIST
S°liquid	143.97	J/mol×K	NIST
Tboil	[145.00; 145.35]	K
Tboil	145.35	K	NCMS SOLV-DB
Tboil	145.00	K	NIST
Tboil	145.12 ± 0.05	K	NIST
Tboil	145.00 ± 1.50	K	NIST
Tboil	145.00 ± 3.00	K	NIST
Tboil	145.10 ± 0.50	K	NIST
Tboil	145.10 ± 0.30	K	NIST
Tboil	145.10 ± 0.50	K	NIST
Tboil	145.15 ± 0.20	K	NIST
Tboil	145.35 ± 0.50	K	NIST
Tc	[227.50; 227.50]	K
Tc	227.50	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	227.50	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	227.50 ± 0.10	K	NIST
Tc	227.50 ± 0.02	K	NIST
Tfus	[86.85; 89.55]	K
Tfus	89.35	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	89.55	K	NCMS SOLV-DB
Tfus	89.00 ± 1.50	K	NIST
Tfus	89.50 ± 0.50	K	NIST
Tfus	86.85 ± 1.00	K	NIST
Ttriple	[88.44; 89.57]	K
Ttriple	89.57	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	89.53 ± 0.02	K	NIST
Ttriple	89.56 ± 0.01	K	NIST
Ttriple	89.52 ± 0.00	K	NIST
Ttriple	89.56 ± 0.02	K	NIST
Ttriple	89.54 ± 0.00	K	NIST
Ttriple	Outlier 88.44 ± 1.00	K	NIST
Ttriple	89.55 ± 0.30	K	NIST
Vc	[0.140; 0.142]	m3/kmol
Vc	0.142	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Vc	0.140	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.142 ± 800.000	m3/kmol	NIST
Zc	0.2760000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	80.08	J/mol×K	145.00	NIST
η	0.0000170	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	[0.69; 1.73]	kJ/mol	[76.10; 89.56]
ΔfusH	1.73	kJ/mol	76.10	NIST
ΔfusH	1.46	kJ/mol	76.10	NIST
ΔfusH	1.71	kJ/mol	76.27	NIST
ΔfusH	0.69	kJ/mol	88.40	NIST
ΔfusH	0.71	kJ/mol	89.50	NIST
ΔfusH	0.71	kJ/mol	89.56	NIST
ΔfusH	0.71	kJ/mol	89.56	NIST
ΔsubH	[14.00; 17.00]	kJ/mol	[76.00; 87.50]
ΔsubH	17.00	kJ/mol	76.00	NIST
ΔsubH	14.00	kJ/mol	83.00	NIST
ΔsubH	14.70	kJ/mol	87.50	NIST
ΔvapH	[11.81; 12.80]	kJ/mol	[119.50; 211.00]
ΔvapH	12.80	kJ/mol	119.50	NIST
ΔvapH	12.30	kJ/mol	126.00	NIST
ΔvapH	12.40	kJ/mol	131.00	NIST
ΔvapH	11.81	kJ/mol	145.12	NIST
ΔvapH	11.90	kJ/mol	178.50	NIST
ΔvapH	12.10	kJ/mol	211.00	NIST
Pvap	[171.92; 2163.00]	kPa	[153.23; 210.03]
Pvap	171.92	kPa	153.23	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	243.00	kPa	159.61	Vapor-Liquid Equilibrium Data of the Methane + Tetrafluoromethane System at Temperatures from (159.61 to 178.93) K
Pvap	269.00	kPa	161.58	Vapor-Liquid Equilibrium Data of the Methane + Tetrafluoromethane System at Temperatures from (159.61 to 178.93) K
Pvap	431.00	kPa	169.38	Vapor-Liquid Equilibrium Data of the Methane + Tetrafluoromethane System at Temperatures from (159.61 to 178.93) K
Pvap	517.00	kPa	173.90	Vapor-Liquid Equilibrium Data of the Methane + Tetrafluoromethane System at Temperatures from (159.61 to 178.93) K
Pvap	651.00	kPa	178.93	Vapor-Liquid Equilibrium Data of the Methane + Tetrafluoromethane System at Temperatures from (159.61 to 178.93) K
Pvap	679.00	kPa	179.68	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
Pvap	1058.00	kPa	190.14	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
Pvap	1205.31	kPa	193.43	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	1575.00	kPa	200.68	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
Pvap	2163.00	kPa	210.03	Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
n0	1.15100		298.15	NCMS SOLV-DB
ΔfusS	[7.70; 22.43]	J/mol×K	[76.10; 89.56]
ΔfusS	21.40	J/mol×K	76.10	NIST
ΔfusS	19.20	J/mol×K	76.10	NIST
ΔfusS	22.43	J/mol×K	76.27	NIST
ΔfusS	7.70	J/mol×K	88.40	NIST
ΔfusS	7.90	J/mol×K	89.50	NIST
ΔfusS	7.95	J/mol×K	89.56	NIST
γ	0.00	N/m	298.15	NCMS SOLV-DB
ΔvapS	81.41	J/mol×K	145.12	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[61.02; 98.82]	J/mol×K	[298.00; 1000.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.59678e+01
Coefficient B			2.10332e+02
Coefficient C			-1.89466e+02
Coefficient D			6.22023e+01
Coefficient E			-2.17317e-01
Reference			Chase, 1998
Comment			F=-946.4877, G=224.6766, H=-933.1994; Data last reviewed in June, 1969
Temperature range, min.			298.00
Temperature range, max.			1000.00
Cp,gas	61.02	J/mol×K	298.00	Calculated Property
Cp,gas	70.04	J/mol×K	376.00	Calculated Property
Cp,gas	77.17	J/mol×K	454.00	Calculated Property
Cp,gas	82.84	J/mol×K	532.00	Calculated Property
Cp,gas	87.30	J/mol×K	610.00	Calculated Property
Cp,gas	90.79	J/mol×K	688.00	Calculated Property
Cp,gas	93.50	J/mol×K	766.00	Calculated Property
Cp,gas	95.62	J/mol×K	844.00	Calculated Property
Cp,gas	97.33	J/mol×K	922.00	Calculated Property
Cp,gas	98.82	J/mol×K	1000.00	Calculated Property
Cp,gas	[98.75; 107.81]	J/mol×K	[1000.00; 6000.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.06222e+02
Coefficient B			1.07612e+00
Coefficient C			-2.23192e-01
Coefficient D			1.57530e-02
Coefficient E			-8.34068e+00
Reference			Chase, 1998
Comment			F=-987.7755, G=355.9764, H=-933.1994; Data last reviewed in June, 1969
Temperature range, min.			1000.00
Temperature range, max.			6000.00
Cp,gas	98.75	J/mol×K	1000.00	Calculated Property
Cp,gas	103.97	J/mol×K	1555.56	Calculated Property
Cp,gas	105.78	J/mol×K	2111.11	Calculated Property
Cp,gas	106.63	J/mol×K	2666.67	Calculated Property
Cp,gas	107.10	J/mol×K	3222.22	Calculated Property
Cp,gas	107.37	J/mol×K	3777.78	Calculated Property
Cp,gas	107.53	J/mol×K	4333.33	Calculated Property
Cp,gas	107.64	J/mol×K	4888.89	Calculated Property
Cp,gas	107.73	J/mol×K	5444.44	Calculated Property
Cp,gas	107.81	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 3735.12]	kPa	[103.48; 227.51]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39902e+01
Coefficient B			-1.23425e+03
Coefficient C			-1.34020e+01
Temperature range, min.			103.48
Temperature range, max.			227.51
Pvap	1.33	kPa	103.48	Calculated Property
Pvap	8.22	kPa	117.26	Calculated Property
Pvap	33.06	kPa	131.04	Calculated Property
Pvap	99.34	kPa	144.82	Calculated Property
Pvap	242.24	kPa	158.60	Calculated Property
Pvap	506.11	kPa	172.39	Calculated Property
Pvap	940.15	kPa	186.17	Calculated Property
Pvap	1593.69	kPa	199.95	Calculated Property
Pvap	2512.34	kPa	213.73	Calculated Property
Pvap	3735.12	kPa	227.51	Calculated Property
Pvap	[13.18; 47.88]	kPa	[121.59; 135.39]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.22504e+01
Coefficient B			-8.67421e+02
Coefficient C			-3.19010e+01
Reference			Regnier, 1972
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			121.59
Temperature range, max.			135.39
Pvap	13.18	kPa	121.59	Calculated Property
Pvap	15.51	kPa	123.12	Calculated Property
Pvap	18.15	kPa	124.66	Calculated Property
Pvap	21.13	kPa	126.19	Calculated Property
Pvap	24.48	kPa	127.72	Calculated Property
Pvap	28.24	kPa	129.26	Calculated Property
Pvap	32.42	kPa	130.79	Calculated Property
Pvap	37.06	kPa	132.32	Calculated Property
Pvap	42.21	kPa	133.86	Calculated Property
Pvap	47.88	kPa	135.39	Calculated Property
Pvap	[0.09; 1.11]	kPa	[89.71; 101.46]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			6.06687e+00
Coefficient B			-2.38497e+02
Coefficient C			-6.14610e+01
Reference			Smith and Pace, 1969
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			89.71
Temperature range, max.			101.46
Pvap	0.09	kPa	89.71	Calculated Property
Pvap	0.13	kPa	91.02	Calculated Property
Pvap	0.19	kPa	92.32	Calculated Property
Pvap	0.26	kPa	93.63	Calculated Property
Pvap	0.35	kPa	94.93	Calculated Property
Pvap	0.45	kPa	96.24	Calculated Property
Pvap	0.58	kPa	97.54	Calculated Property
Pvap	0.73	kPa	98.85	Calculated Property
Pvap	0.91	kPa	100.15	Calculated Property
Pvap	1.11	kPa	101.46	Calculated Property
Pvap	[0.20; 106.65]	kPa	[92.51; 145.87]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42028e+01
Coefficient B			-1.28166e+03
Coefficient C			-1.14300e+01
Reference			Menzel and Mohry, 1933
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			92.51
Temperature range, max.			145.87
Pvap	0.20	kPa	92.51	Calculated Property
Pvap	0.59	kPa	98.44	Calculated Property
Pvap	1.51	kPa	104.37	Calculated Property
Pvap	3.45	kPa	110.30	Calculated Property
Pvap	7.19	kPa	116.23	Calculated Property
Pvap	13.84	kPa	122.15	Calculated Property
Pvap	24.93	kPa	128.08	Calculated Property
Pvap	42.41	kPa	134.01	Calculated Property
Pvap	68.70	kPa	139.94	Calculated Property
Pvap	106.65	kPa	145.87	Calculated Property

Similar Compounds

Find more compounds similar to Tetrafluoromethane.

Mixtures

• 2-PROPANOL, 1,1,1,3,3,3-HEXAFLUORO- + Tetrafluoromethane + Water
• Tetrafluoromethane + Furan, tetrahydro-2,5-dimethyl- + Furan, tetrahydro-2,5-dimethyl-, cis-
• Tetrafluoromethane + Methyl Alcohol
• Tetrafluoromethane + Ethanol
• 1-Propanol + Tetrafluoromethane
• Tetrafluoromethane + 1-Butanol
• Benzene + Tetrafluoromethane
• Toluene + Tetrafluoromethane
• Tetrafluoromethane + Benzene, 1,3-dimethyl-
• Tetrafluoromethane + Mesitylene
• Hexane, tetradecafluoro- + Tetrafluoromethane
• Tetrafluoromethane + Octadecafluorooctane
• Ethanol, 2,2,2-trifluoro- + Tetrafluoromethane + Water
• 2,5,8,11-Tetraoxadodecane + Tetrafluoromethane
• Tetrafluoromethane + 2,5,8,11,14-Pentaoxapentadecane
• Tetrafluoromethane + Carbonic acid, dimethyl ester
• Diethyl carbonate + Tetrafluoromethane
• Nitrogen + Tetrafluoromethane
• Tetrafluoromethane + Ethane
• Propane + Tetrafluoromethane

Find more mixtures with Tetrafluoromethane.

Sources

• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• Cheméo Relay (1.0)
• Crippen Method
• Solubility of CF4 in lower alcohols
• Solubilities of several non-polar gases in mixtures water + 2,2,2-trifluoroethanol at 298.15 K and 101.33 kPa
• Solubility of hydrofluorocarbons in aromatic solvents and alcohols: Experimental data and modeling with CPA EoS
• 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)
• VLE measurements and modelling for the binary systems of (CF4 + C6F14) and (CF4 + C8F18)
• 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
• 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
• Isothermal Vapor-Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) K
• Vapor-Liquid Equilibrium Data of the Methane + Tetrafluoromethane System at Temperatures from (159.61 to 178.93) K
• Vapor Liquid Equilibrium Measurements for a Tetrafluoromethane + Propane System over a Temperature Range from (142.96 to 293.23) K
• Solubility of Hydrofluorocarbons in Halobenzene Solvents
• Vapor-Liquid Equilibrium Measurements for the Nitrogen + Tetrafluoromethane System over a Temperature Range of (134.27 to 204.85) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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