Chemical Properties of Sulfur hexafluoride (CAS 2551-62-4)

InChI

InChI=1S/F6S/c1-7(2,3,4,5)6

InChI Key

SFZCNBIFKDRMGX-UHFFFAOYSA-N

Formula

F6S

SMILES

FS(F)(F)(F)(F)F

Molecular Weight¹

146.06

CAS

2551-62-4

Other Names

• Elegas
• Esaflon
• Hexafluorure de soufre
• OC-6-11
• SF6
• Sulfur fluoride
• UN 1080
• sulphur hexafluoride

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (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).
• EA : Electron affinity (eV).
• 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 a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• 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).
• ρ_c : Critical density (kg/m³).
• ρ_g : Gas Density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.1499; 0.2080]
ω	0.1499		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2080		ChemSep v8.3 pure component data Compiled value
PAff	575.30	kJ/mol	NIST
BasG	[550.70; 575.30]	kJ/mol
BasG	550.70	kJ/mol	NIST
BasG	575.30	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
EA	[0.32; 3.16]	eV
EA	0.91 ± 0.07	eV	NIST
EA	1.03 ± 0.05	eV	NIST
EA	1.07 ± 0.07	eV	NIST
EA	1.15 ± 0.15	eV	NIST
EA	1.05 ± 0.10	eV	NIST
EA	1.39 ± 0.13	eV	NIST
EA	0.80	eV	NIST
EA	1.20 ± 0.30	eV	NIST
EA	0.54	eV	NIST
EA	0.93	eV	NIST
EA	Outlier 2.60 ± 0.10	eV	NIST
EA	Outlier 2.60 ± 0.10	eV	NIST
EA	Outlier 3.16	eV	NIST
EA	0.70	eV	NIST
EA	0.46 ± 0.20	eV	NIST
EA	0.75 ± 0.10	eV	NIST
EA	0.54 ± 0.17	eV	NIST
EA	0.53 ± 0.10	eV	NIST
EA	0.60 ± 0.10	eV	NIST
EA	0.95 ± 0.52	eV	NIST
EA	0.43	eV	NIST
EA	0.70	eV	NIST
EA	1.10	eV	NIST
EA	0.32 ± 0.15	eV	NIST
EA	1.49 ± 0.22	eV	NIST
ΔfG°	-1105.30	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-1209.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	11.64	kJ/mol	Joback Calculated Property
ΔvapH	23.69	kJ/mol	Air Liquide Gas Encyclopedia
IE	[15.30; 15.81]	eV
IE	15.32 ± 0.02	eV	NIST
IE	15.30	eV	NIST
IE	15.30	eV	NIST
IE	15.35 ± 0.02	eV	NIST
IE	15.70	eV	NIST
IE	15.70	eV	NIST
IE	15.69	eV	NIST
IE	15.81	eV	NIST
logPoct/wat	3.169		Crippen Calculated Property
McVol	46.430	ml/mol	McGowan Calculated Property
Pc	[2490.00; 3760.17]	kPa
Pc	3759.16	kPa	Mathews (1972), critical constants of inorganic substances Compiled value
Pc	3760.17	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3760.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3755.00	kPa	Air Liquide Gas Encyclopedia
Pc	Outlier 2490.00 ± 30.00	kPa	NIST
Pc	3758.60 ± 0.50	kPa	NIST
Ptriple	[225.05; 232.67]	kPa
Ptriple	225.05	kPa	Staveley, Lobo and Calado (1981), triple points Compiled value
Ptriple	232.67	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	231.40	kPa	Air Liquide Gas Encyclopedia
ρc	[738.76; 751.75]	kg/m3
ρc	742.30	kg/m3	Air Liquide Gas Encyclopedia
ρc	738.76 ± 0.15	kg/m3	NIST
ρc	751.75 ± 0.58	kg/m3	NIST
Inp	[135.00; 135.00]
Inp	135.00		NIST
Inp	135.00		NIST
Tboil	[209.25; 209.30]	K
Tboil	209.25	K	ChemSep v8.3 pure component data Compiled value
Tboil	209.30	K	NIST
Tc	[318.69; 591.85]	K
Tc	318.69	K	Mathews (1972), critical constants of inorganic substances Compiled value
Tc	318.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	318.72	K	ChemSep v8.3 pure component data Compiled value
Tc	318.72	K	Air Liquide Gas Encyclopedia
Tc	568.80 ± 0.70	K	NIST
Tc	318.72	K	NIST
Tc	318.71 ± 0.01	K	NIST
Tc	318.76	K	NIST
Tc	591.85 ± 0.05	K	NIST
Tfus	[222.35; 222.65]	K
Tfus	222.35	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	222.65	K	ChemSep v8.3 pure component data Compiled value
Tfus	222.45	K	Air Liquide Gas Encyclopedia
Ttriple	[222.41; 223.72]	K
Ttriple	222.41	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	223.15	K	ChemSep v8.3 pure component data Compiled value
Ttriple	223.55	K	Air Liquide Gas Encyclopedia
Ttriple	223.72 ± 0.01	K	NIST
UQi	3.28		ChemSep v8.3 pure component data Compiled value
URi	3.09		ChemSep v8.3 pure component data Compiled value
Vc	[0.197; 0.199]	m3/kmol
Vc	0.198	m3/kmol	Mathews (1972), critical constants of inorganic substances Compiled value
Vc	0.199	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.198	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.198 ± 0.000	m3/kmol	NIST
Vc	0.197	m3/kmol	NIST
Zc	[0.2670000; 0.2820000]
Zc	0.2670000		Mathews (1972), critical constants of inorganic substances Compiled value
Zc	0.2820000		ChemSep v8.3 pure component data Compiled value
Zra	0.28		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Enthalpy of vaporization at standard conditions, 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
ΔfusH	5.02	kJ/mol	222.45	Air Liquide Gas Encyclopedia
ΔsubH	[23.20; 23.30]	kJ/mol	[186.00; 191.00]
ΔsubH	23.20 ± 0.01	kJ/mol	186.00	NIST
ΔsubH	23.30	kJ/mol	191.00	NIST
ρg	6.26	kg/m3	288.15	Air Liquide Gas Encyclopedia

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Viscosity, Pa*s - Gas
300.00	26.36	0.0000
300.00	50.94	0.0000
300.00	73.62	0.0000
300.00	105.89	0.0000
300.00	125.70	0.0000
300.00	152.62	0.0000
300.00	177.62	0.0000
300.00	195.25	0.0000
300.00	227.52	0.0000
300.00	251.51	0.0000
300.00	278.58	0.0000
300.00	301.45	0.0000
300.00	327.30	0.0000
300.00	353.41	0.0000
300.00	378.55	0.0000
300.00	401.57	0.0000
300.00	425.72	0.0000
300.00	444.52	0.0000
300.00	471.71	0.0000
300.00	491.53	0.0000
300.00	538.31	0.0000
300.00	565.24	0.0000
300.00	597.98	0.0000
300.00	634.58	0.0000
300.00	665.10	0.0000
300.00	700.96	0.0000
300.00	731.45	0.0000
300.00	763.98	0.0000
300.00	800.20	0.0000
300.00	835.89	0.0000
300.00	869.95	0.0000
300.00	898.41	0.0000
300.00	930.75	0.0000
300.00	968.74	0.0000
300.00	997.76	0.0000
300.00	1036.40	0.0000
300.00	1090.20	0.0000
300.00	1140.10	0.0000
300.00	1181.50	0.0000
300.00	1223.60	0.0000
300.00	1280.60	0.0000
300.00	1333.30	0.0000
300.00	1380.90	0.0000
300.00	1417.90	0.0000
300.00	1493.30	0.0000
300.00	1537.70	0.0000
300.00	1594.60	0.0000
300.00	1637.30	0.0000
300.00	1680.60	0.0000
300.00	1735.30	0.0000
300.00	1784.40	0.0000
300.00	1826.50	0.0000
300.00	1865.10	0.0000
300.00	1927.30	0.0000
300.00	1980.00	0.0000
300.00	2039.30	0.0000
316.00	112.75	0.0000
316.00	143.54	0.0000
316.00	174.60	0.0000
316.00	197.59	0.0000
316.00	218.05	0.0000
316.00	245.03	0.0000
316.00	262.84	0.0000
316.00	287.46	0.0000
316.00	307.35	0.0000
316.00	332.06	0.0000
316.00	357.70	0.0000
316.00	383.76	0.0000
316.00	402.43	0.0000
316.00	428.01	0.0000
316.00	468.39	0.0000
316.00	490.91	0.0000
316.00	519.48	0.0000
316.00	548.34	0.0000
316.00	585.01	0.0000
316.00	614.48	0.0000
316.00	650.85	0.0000
316.00	685.07	0.0000
316.00	712.63	0.0000
316.00	749.05	0.0000
316.00	780.40	0.0000
316.00	810.74	0.0000
316.00	843.20	0.0000
316.00	882.81	0.0000
316.00	913.90	0.0000
316.00	955.92	0.0000
316.00	994.72	0.0000
316.00	1031.10	0.0000
316.00	1084.10	0.0000
316.00	1120.40	0.0000
316.00	1178.30	0.0000
316.00	1215.20	0.0000
316.00	1257.30	0.0000
316.00	1314.30	0.0000
316.00	1374.40	0.0000
316.00	1422.90	0.0000
316.00	1465.60	0.0000
316.00	1530.40	0.0000
316.00	1572.70	0.0000
316.00	1609.80	0.0000
316.00	1667.20	0.0000
316.00	1724.20	0.0000
316.00	1772.50	0.0000
316.00	1821.10	0.0000
316.00	1860.30	0.0000
316.00	1922.70	0.0000
316.00	1988.50	0.0000
316.00	2021.60	0.0000
316.00	2087.40	0.0000
316.00	2155.20	0.0000
316.00	2223.80	0.0000
316.00	2273.20	0.0000
316.00	2319.10	0.0000
316.00	2375.80	0.0000
316.00	2448.50	0.0000
316.00	2510.00	0.0000
316.00	2587.20	0.0000
316.00	2658.20	0.0000
316.00	2724.30	0.0000
316.00	2792.70	0.0000
316.00	2860.90	0.0000
316.00	2916.50	0.0000
316.00	2981.10	0.0000
316.00	3007.90	0.0000
316.00	3070.00	0.0000
316.00	3135.20	0.0000
321.00	77.46	0.0000
321.00	97.02	0.0000
321.00	114.16	0.0000
321.00	146.57	0.0000
321.00	169.96	0.0000
321.00	205.62	0.0000
321.00	239.58	0.0000
321.00	264.10	0.0000
321.00	293.39	0.0000
321.00	339.65	0.0000
321.00	374.89	0.0000
321.00	400.93	0.0000
321.00	428.98	0.0000
321.00	457.31	0.0000
321.00	488.99	0.0000
321.00	523.86	0.0000
321.00	563.16	0.0000
321.00	592.18	0.0000
321.00	633.22	0.0000
321.00	681.18	0.0000
321.00	732.46	0.0000
321.00	790.88	0.0000
321.00	823.55	0.0000
321.00	857.52	0.0000
321.00	896.20	0.0000
321.00	934.23	0.0000
321.00	969.00	0.0000
321.00	1031.40	0.0000
321.00	1089.40	0.0000
321.00	1125.00	0.0000
321.00	1178.70	0.0000
321.00	1223.20	0.0000
321.00	1282.40	0.0000
321.00	1340.00	0.0000
321.00	1386.20	0.0000
321.00	1431.80	0.0000
321.00	1483.30	0.0000
321.00	1538.90	0.0000
321.00	1647.00	0.0000
321.00	1693.10	0.0000
321.00	1744.50	0.0000
321.00	1788.60	0.0000
321.00	1847.40	0.0000
321.00	1893.80	0.0000
321.00	1930.70	0.0000
321.00	2004.90	0.0000
321.00	2041.90	0.0000
321.00	2120.40	0.0000
321.00	2221.30	0.0000
321.00	2270.30	0.0000
321.00	2332.70	0.0000
321.00	2373.20	0.0000
321.00	2451.30	0.0000
321.00	2534.70	0.0000
321.00	2581.90	0.0000
321.00	2629.50	0.0000
321.00	2688.10	0.0000
321.00	2803.90	0.0000
321.00	2873.50	0.0000
321.00	2959.10	0.0000
321.00	3050.00	0.0000
321.00	3136.60	0.0000
321.00	3229.60	0.0000
321.00	3282.00	0.0000
321.00	3384.40	0.0000
321.00	3445.90	0.0000
321.00	3498.80	0.0000
321.00	3558.30	0.0000
321.00	3606.10	0.0000
321.00	3651.40	0.0000
321.00	3695.60	0.0000
321.00	3729.20	0.0000
321.00	3765.40	0.0000
321.00	3793.60	0.0000
321.00	3819.60	0.0000
321.00	3858.50	0.0000
321.00	3887.80	0.0000
321.00	3899.40	0.0000
321.00	3910.10	0.0000
321.00	3918.40	0.0000
321.00	3926.60	0.0000
321.00	3933.30	0.0000
321.00	3938.40	0.0000
321.00	3945.70	0.0000
321.00	3950.60	0.0000
321.00	3955.40	0.0000
321.00	3961.00	0.0000
321.00	3968.80	0.0000
321.00	3977.00	0.0000
321.00	3988.30	0.0001
321.00	4001.10	0.0001
321.00	4020.80	0.0001
321.00	4046.80	0.0001
321.00	4077.10	0.0001
321.00	4112.90	0.0001
321.00	4160.00	0.0001
321.00	4223.80	0.0001
321.00	4349.40	0.0001
321.00	4465.50	0.0001
321.00	4601.30	0.0001
321.00	4740.50	0.0001
321.00	4879.10	0.0001
321.00	5134.00	0.0001
321.00	5554.10	0.0001
321.00	5938.00	0.0001
321.00	6388.70	0.0001
321.00	7256.20	0.0001
321.00	7905.10	0.0001
321.00	8647.50	0.0001
321.00	9548.10	0.0001
321.00	10352.00	0.0001
321.00	11075.00	0.0001
333.15	91.55	0.0000
333.15	113.58	0.0000
333.15	142.52	0.0000
333.15	172.42	0.0000
333.15	198.48	0.0000
333.15	218.78	0.0000
333.15	243.22	0.0000
333.15	275.20	0.0000
333.15	294.03	0.0000
333.15	319.41	0.0000
333.15	350.89	0.0000
333.15	378.94	0.0000
333.15	416.93	0.0000
333.15	443.40	0.0000
333.15	479.64	0.0000
333.15	506.60	0.0000
333.15	547.64	0.0000
333.15	590.65	0.0000
333.15	636.15	0.0000
333.15	671.18	0.0000
333.15	717.74	0.0000
333.15	772.31	0.0000
333.15	837.79	0.0000
333.15	887.92	0.0000
333.15	946.43	0.0000
333.15	1025.70	0.0000
333.15	1092.50	0.0000
333.15	1167.40	0.0000
333.15	1233.20	0.0000
333.15	1307.80	0.0000
333.15	1366.90	0.0000
333.15	1419.70	0.0000
333.15	1502.80	0.0000
333.15	1566.40	0.0000
333.15	1629.70	0.0000
333.15	1705.80	0.0000
333.15	1772.90	0.0000
333.15	1853.50	0.0000
333.15	1917.40	0.0000
333.15	1967.00	0.0000
333.15	2025.70	0.0000
333.15	2294.70	0.0000
333.15	2427.70	0.0000
333.15	2519.20	0.0000
333.15	2631.90	0.0000
333.15	2766.30	0.0000
333.15	2872.00	0.0000
333.15	3008.30	0.0000
333.15	3089.40	0.0000
333.15	3195.20	0.0000
333.15	3306.10	0.0000
333.15	3398.70	0.0000
333.15	3504.00	0.0000
333.15	3605.10	0.0000
333.15	3722.00	0.0000
333.15	3815.40	0.0000
333.15	3932.10	0.0000
333.15	4050.80	0.0000
333.15	4148.20	0.0000
333.15	4239.90	0.0000
333.15	4328.20	0.0000
333.15	4406.90	0.0000
333.15	4479.70	0.0000
333.15	4549.60	0.0000
333.15	4612.30	0.0000
333.15	4671.80	0.0000
333.15	4725.80	0.0000
333.15	4776.60	0.0000
333.15	4828.10	0.0000
333.15	4880.10	0.0000
333.15	4933.20	0.0000
333.15	4991.60	0.0000
333.15	5049.00	0.0000
333.15	5109.40	0.0000
333.15	5178.80	0.0000
333.15	5254.90	0.0001
333.15	5343.60	0.0001
333.15	5447.50	0.0001
333.15	5567.40	0.0001
333.15	5709.90	0.0001
333.15	5869.50	0.0001
333.15	6098.20	0.0001
333.15	6338.20	0.0001
333.15	6627.70	0.0001
333.15	6950.60	0.0001
333.15	7378.30	0.0001
333.15	7900.00	0.0001
333.15	8519.80	0.0001
333.15	9106.80	0.0001
333.15	9802.00	0.0001
333.15	10465.00	0.0001
333.15	11412.00	0.0001
333.15	12565.00	0.0001
350.00	64.67	0.0000
350.00	96.54	0.0000
350.00	117.61	0.0000
350.00	143.77	0.0000
350.00	170.68	0.0000
350.00	204.56	0.0000
350.00	238.01	0.0000
350.00	269.03	0.0000
350.00	295.24	0.0000
350.00	332.44	0.0000
350.00	363.13	0.0000
350.00	390.50	0.0000
350.00	418.50	0.0000
350.00	450.38	0.0000
350.00	485.30	0.0000
350.00	522.75	0.0000
350.00	552.81	0.0000
350.00	579.70	0.0000
350.00	619.51	0.0000
350.00	654.26	0.0000
350.00	701.64	0.0000
350.00	739.48	0.0000
350.00	779.89	0.0000
350.00	809.98	0.0000
350.00	855.04	0.0000
350.00	900.26	0.0000
350.00	954.25	0.0000
350.00	997.88	0.0000
350.00	1051.50	0.0000
350.00	1146.20	0.0000
350.00	1196.50	0.0000
350.00	1265.40	0.0000
350.00	1341.20	0.0000
350.00	1392.70	0.0000
350.00	1473.10	0.0000
350.00	1546.10	0.0000
350.00	1621.80	0.0000
350.00	1656.30	0.0000
350.00	1713.20	0.0000
350.00	1840.00	0.0000
350.00	1888.30	0.0000
350.00	1964.60	0.0000
350.00	2005.90	0.0000
350.00	2043.20	0.0000
350.00	2108.60	0.0000
350.00	2309.30	0.0000
350.00	2394.00	0.0000
350.00	2449.20	0.0000
350.00	2505.10	0.0000
350.00	2608.10	0.0000
350.00	2657.70	0.0000
350.00	2798.40	0.0000
350.00	2900.40	0.0000
350.00	2978.20	0.0000
350.00	3047.10	0.0000
350.00	3125.30	0.0000
350.00	3224.50	0.0000
350.00	3319.60	0.0000
350.00	3405.30	0.0000
350.00	3504.40	0.0000
350.00	3655.40	0.0000
350.00	3748.00	0.0000
350.00	3869.50	0.0000
350.00	3987.50	0.0000
350.00	4143.00	0.0000
350.00	4307.30	0.0000
350.00	4473.20	0.0000
350.00	4598.10	0.0000
350.00	4732.90	0.0000
350.00	4848.30	0.0000
350.00	4964.30	0.0000
350.00	5096.10	0.0000
350.00	5208.70	0.0000
350.00	5327.40	0.0000
350.00	5431.30	0.0000
350.00	5524.20	0.0000
350.00	5638.80	0.0000
350.00	5741.00	0.0000
350.00	5850.00	0.0000
350.00	5956.20	0.0000
350.00	6067.60	0.0000
350.00	6177.60	0.0000
350.00	6280.80	0.0000
350.00	6385.10	0.0000
350.00	6510.80	0.0000
350.00	6635.40	0.0000
350.00	6769.60	0.0000
350.00	6918.80	0.0000
350.00	7076.50	0.0001
350.00	7230.00	0.0001
350.00	7408.10	0.0001
350.00	7592.00	0.0001
350.00	7767.30	0.0001
350.00	8006.20	0.0001
350.00	8297.40	0.0001
350.00	8558.70	0.0001
350.00	8849.50	0.0001
350.00	9294.00	0.0001
350.00	9823.40	0.0001
350.00	10614.00	0.0001
350.00	11424.00	0.0001
350.00	12301.00	0.0001
375.00	72.56	0.0000
375.00	103.02	0.0000
375.00	132.08	0.0000
375.00	156.74	0.0000
375.00	183.32	0.0000
375.00	219.98	0.0000
375.00	258.30	0.0000
375.00	282.80	0.0000
375.00	308.36	0.0000
375.00	342.15	0.0000
375.00	371.36	0.0000
375.00	403.52	0.0000
375.00	435.36	0.0000
375.00	464.82	0.0000
375.00	499.73	0.0000
375.00	539.14	0.0000
375.00	563.93	0.0000
375.00	612.98	0.0000
375.00	661.40	0.0000
375.00	695.12	0.0000
375.00	746.70	0.0000
375.00	805.08	0.0000
375.00	855.26	0.0000
375.00	917.96	0.0000
375.00	999.57	0.0000
375.00	1067.60	0.0000
375.00	1146.80	0.0000
375.00	1211.30	0.0000
375.00	1302.50	0.0000
375.00	1385.00	0.0000
375.00	1460.90	0.0000
375.00	1534.40	0.0000
375.00	1588.30	0.0000
375.00	1723.30	0.0000
375.00	1809.50	0.0000
375.00	1885.10	0.0000
375.00	1966.60	0.0000
375.00	2043.00	0.0000
375.00	2300.60	0.0000
375.00	2399.30	0.0000
375.00	2484.30	0.0000
375.00	2587.30	0.0000
375.00	2879.20	0.0000
375.00	3052.50	0.0000
375.00	3214.10	0.0000
375.00	3418.40	0.0000
375.00	3699.70	0.0000
375.00	3960.70	0.0000
375.00	4136.60	0.0000
375.00	4384.30	0.0000
375.00	4599.00	0.0000
375.00	4821.00	0.0000
375.00	5057.00	0.0000
375.00	5280.90	0.0000
375.00	5535.40	0.0000
375.00	5778.60	0.0000
375.00	6000.40	0.0000
375.00	6326.20	0.0000
375.00	6677.70	0.0000
375.00	6887.60	0.0000
375.00	7092.90	0.0000
375.00	7293.50	0.0000
375.00	7524.40	0.0000
375.00	7762.90	0.0000
375.00	7973.10	0.0000
375.00	8202.00	0.0000
375.00	8452.70	0.0000
375.00	8711.30	0.0000
375.00	8972.90	0.0000
375.00	9257.70	0.0000
375.00	9573.70	0.0001
375.00	9868.90	0.0001
375.00	10221.00	0.0001
375.00	10547.00	0.0001
375.00	11030.00	0.0001
375.00	11466.00	0.0001
375.00	12235.00	0.0001
375.00	12730.00	0.0001
375.00	13213.00	0.0001
375.00	13867.00	0.0001
375.00	14447.00	0.0001
375.00	15713.00	0.0001
375.00	16802.00	0.0001
400.00	100.75	0.0000
400.00	127.69	0.0000
400.00	153.61	0.0000
400.00	174.48	0.0000
400.00	200.50	0.0000
400.00	224.70	0.0000
400.00	249.97	0.0000
400.00	276.92	0.0000
400.00	316.57	0.0000
400.00	356.06	0.0000
400.00	387.16	0.0000
400.00	431.42	0.0000
400.00	458.70	0.0000
400.00	482.84	0.0000
400.00	520.38	0.0000
400.00	569.64	0.0000
400.00	636.33	0.0000
400.00	669.90	0.0000
400.00	702.50	0.0000
400.00	753.74	0.0000
400.00	791.41	0.0000
400.00	818.44	0.0000
400.00	853.97	0.0000
400.00	930.59	0.0000
400.00	972.98	0.0000
400.00	1025.60	0.0000
400.00	1088.20	0.0000
400.00	1153.30	0.0000
400.00	1240.90	0.0000
400.00	1319.70	0.0000
400.00	1397.40	0.0000
400.00	1462.50	0.0000
400.00	1615.70	0.0000
400.00	1688.50	0.0000
400.00	1768.00	0.0000
400.00	1876.40	0.0000
400.00	1956.00	0.0000
400.00	2349.80	0.0000
400.00	2474.20	0.0000
400.00	2539.40	0.0000
400.00	2835.40	0.0000
400.00	3021.70	0.0000
400.00	3266.30	0.0000
400.00	3463.70	0.0000
400.00	3614.20	0.0000
400.00	3864.10	0.0000
400.00	4152.90	0.0000
400.00	4564.10	0.0000
400.00	4898.50	0.0000
400.00	5193.20	0.0000
400.00	5460.70	0.0000
400.00	5742.70	0.0000
400.00	6016.60	0.0000
400.00	6359.60	0.0000
400.00	6659.90	0.0000
400.00	6950.70	0.0000
400.00	7241.00	0.0000
400.00	7553.00	0.0000
400.00	7833.90	0.0000
400.00	8142.00	0.0000
400.00	8490.60	0.0000
400.00	8799.00	0.0000
400.00	9139.90	0.0000
400.00	9483.50	0.0000
400.00	9833.20	0.0000
400.00	10191.00	0.0000
400.00	10589.00	0.0000
400.00	11000.00	0.0000
400.00	11434.00	0.0000
400.00	11902.00	0.0001
400.00	12397.00	0.0001
400.00	12979.00	0.0001
400.00	13719.00	0.0001
400.00	14342.00	0.0001
400.00	15061.00	0.0001
400.00	15882.00	0.0001
400.00	16792.00	0.0001
400.00	17814.00	0.0001
400.00	18718.00	0.0001
400.00	19958.00	0.0001
425.00	94.41	0.0000
425.00	120.34	0.0000
425.00	155.20	0.0000
425.00	171.36	0.0000
425.00	192.07	0.0000
425.00	205.12	0.0000
425.00	228.29	0.0000
425.00	263.75	0.0000
425.00	289.54	0.0000
425.00	311.35	0.0000
425.00	345.33	0.0000
425.00	374.10	0.0000
425.00	392.73	0.0000
425.00	424.79	0.0000
425.00	466.85	0.0000
425.00	503.16	0.0000
425.00	552.86	0.0000
425.00	598.07	0.0000
425.00	629.86	0.0000
425.00	668.63	0.0000
425.00	715.37	0.0000
425.00	764.24	0.0000
425.00	813.31	0.0000
425.00	867.54	0.0000
425.00	939.66	0.0000
425.00	997.00	0.0000
425.00	1067.10	0.0000
425.00	1141.50	0.0000
425.00	1213.40	0.0000
425.00	1299.40	0.0000
425.00	1385.60	0.0000
425.00	1442.80	0.0000
425.00	1506.30	0.0000
425.00	1587.60	0.0000
425.00	1656.30	0.0000
425.00	1757.60	0.0000
425.00	1833.50	0.0000
425.00	1920.50	0.0000
425.00	2344.20	0.0000
425.00	2479.60	0.0000
425.00	2578.50	0.0000
425.00	2931.10	0.0000
425.00	3150.40	0.0000
425.00	3325.50	0.0000
425.00	3586.10	0.0000
425.00	3797.10	0.0000
425.00	4066.40	0.0000
425.00	4298.80	0.0000
425.00	4546.20	0.0000
425.00	4863.60	0.0000
425.00	5124.60	0.0000
425.00	5454.20	0.0000
425.00	5739.40	0.0000
425.00	6056.40	0.0000
425.00	6339.50	0.0000
425.00	6654.30	0.0000
425.00	7006.00	0.0000
425.00	7363.20	0.0000
425.00	7712.70	0.0000
425.00	8064.10	0.0000
425.00	8392.30	0.0000
425.00	8760.70	0.0000
425.00	9135.40	0.0000
425.00	9514.50	0.0000
425.00	9876.10	0.0000
425.00	10296.00	0.0000
425.00	10899.00	0.0000
425.00	11563.00	0.0000
425.00	11725.00	0.0000
425.00	12199.00	0.0000
425.00	12731.00	0.0000
425.00	13246.00	0.0000
425.00	14152.00	0.0001
425.00	14767.00	0.0001
425.00	15462.00	0.0001
425.00	16201.00	0.0001
425.00	17025.00	0.0001
425.00	17904.00	0.0001
425.00	18751.00	0.0001
425.00	19579.00	0.0001
425.00	20442.00	0.0001
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[38.54; 154.60]	J/mol×K	[100.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.23220e+01
Coefficient B			-3.68100e+02
Coefficient C			5.57024e+00
Coefficient D			-6.33260e-04
Coefficient E			1.91690e-07
Temperature range, min.			100.00
Temperature range, max.			1500.00
Cp,gas	38.54	J/mol×K	100.00	Calculated Property
Cp,gas	85.87	J/mol×K	255.56	Calculated Property
Cp,gas	117.69	J/mol×K	411.11	Calculated Property
Cp,gas	134.16	J/mol×K	566.67	Calculated Property
Cp,gas	142.62	J/mol×K	722.22	Calculated Property
Cp,gas	147.07	J/mol×K	877.78	Calculated Property
Cp,gas	149.57	J/mol×K	1033.33	Calculated Property
Cp,gas	151.27	J/mol×K	1188.89	Calculated Property
Cp,gas	152.81	J/mol×K	1344.44	Calculated Property
Cp,gas	154.60	J/mol×K	1500.00	Calculated Property
Cp,gas	[96.88; 149.32]	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			5.89032e+01
Coefficient B			2.55540e+02
Coefficient C			-2.52275e+02
Coefficient D			8.87606e+01
Coefficient E			-1.60897e+00
Reference			Chase, 1998
Comment			F=-1252.744, G=287.9914, H=-1220.473; Data last reviewed in June, 1976
Temperature range, min.			298.00
Temperature range, max.			1000.00
Cp,gas	96.88	J/mol×K	298.00	Calculated Property
Cp,gas	112.66	J/mol×K	376.00	Calculated Property
Cp,gas	123.42	J/mol×K	454.00	Calculated Property
Cp,gas	131.13	J/mol×K	532.00	Calculated Property
Cp,gas	136.73	J/mol×K	610.00	Calculated Property
Cp,gas	140.81	J/mol×K	688.00	Calculated Property
Cp,gas	143.77	J/mol×K	766.00	Calculated Property
Cp,gas	145.98	J/mol×K	844.00	Calculated Property
Cp,gas	147.73	J/mol×K	922.00	Calculated Property
Cp,gas	149.32	J/mol×K	1000.00	Calculated Property
Cp,gas	[149.25; 157.73]	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			1.57139e+02
Coefficient B			4.84022e-01
Coefficient C			-1.00724e-01
Coefficient D			7.12700e-03
Coefficient E			-8.27964e+00
Reference			Chase, 1998
Comment			F=-1291.990, G=443.2111, H=-1220.473; Data last reviewed in June, 1976
Temperature range, min.			1000.00
Temperature range, max.			6000.00
Cp,gas	149.25	J/mol×K	1000.00	Calculated Property
Cp,gas	154.25	J/mol×K	1555.56	Calculated Property
Cp,gas	155.92	J/mol×K	2111.11	Calculated Property
Cp,gas	156.68	J/mol×K	2666.67	Calculated Property
Cp,gas	157.09	J/mol×K	3222.22	Calculated Property
Cp,gas	157.33	J/mol×K	3777.78	Calculated Property
Cp,gas	157.48	J/mol×K	4333.33	Calculated Property
Cp,gas	157.58	J/mol×K	4888.89	Calculated Property
Cp,gas	157.66	J/mol×K	5444.44	Calculated Property
Cp,gas	157.73	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[119.50; 119.50]	J/mol×K	[230.15; 239.65]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.19500e+02
Coefficient B			-2.04000e+03
Coefficient C			-1.64329e+01
Coefficient D			5.21600e-03
Coefficient E			-4.46910e-05
Temperature range, min.			230.15
Temperature range, max.			239.65
Cp,liquid	119.50	J/mol×K	230.15	Calculated Property
Cp,liquid	119.50	J/mol×K	231.21	Calculated Property
Cp,liquid	119.50	J/mol×K	232.26	Calculated Property
Cp,liquid	119.50	J/mol×K	233.32	Calculated Property
Cp,liquid	119.50	J/mol×K	234.37	Calculated Property
Cp,liquid	119.50	J/mol×K	235.43	Calculated Property
Cp,liquid	119.50	J/mol×K	236.48	Calculated Property
Cp,liquid	119.50	J/mol×K	237.54	Calculated Property
Cp,liquid	119.50	J/mol×K	238.59	Calculated Property
Cp,liquid	119.50	J/mol×K	239.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0005378; 0.0002388]	Pa×s	[223.15; 318.69]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			2.09590e+01
Coefficient B			-4.57460e+02
Coefficient C			-4.94860e+00
Coefficient D			6.51050e-06
Coefficient E			2.00000e+00
Temperature range, min.			223.15
Temperature range, max.			318.69
η	0.0005378	Pa×s	223.15	Calculated Property
η	0.0004840	Pa×s	233.77	Calculated Property
η	0.0004372	Pa×s	244.38	Calculated Property
η	0.0003964	Pa×s	255.00	Calculated Property
η	0.0003608	Pa×s	265.61	Calculated Property
η	0.0003296	Pa×s	276.23	Calculated Property
η	0.0003023	Pa×s	286.84	Calculated Property
η	0.0002784	Pa×s	297.46	Calculated Property
η	0.0002573	Pa×s	308.07	Calculated Property
η	0.0002388	Pa×s	318.69	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[16.18; 0.00]	kJ/mol	[223.15; 318.72]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			5.07690e+01
Coefficient B			8.56050e+00
Coefficient C			-2.57090e+01
Coefficient D			2.94370e+01
Coefficient E			-1.17740e+01
Critical temperature, Tc (K)			3.18720e+02
Comment			Range stopped at Tc; ChemSep gives it to 318.75 K.
Temperature range, min.			223.15
Temperature range, max.			318.72
ΔvapH	16.18	kJ/mol	223.15	Calculated Property
ΔvapH	15.56	kJ/mol	233.77	Calculated Property
ΔvapH	14.80	kJ/mol	244.39	Calculated Property
ΔvapH	13.90	kJ/mol	255.01	Calculated Property
ΔvapH	12.89	kJ/mol	265.63	Calculated Property
ΔvapH	11.77	kJ/mol	276.24	Calculated Property
ΔvapH	10.53	kJ/mol	286.86	Calculated Property
ΔvapH	9.08	kJ/mol	297.48	Calculated Property
ΔvapH	7.05	kJ/mol	308.10	Calculated Property
ΔvapH	0.00	kJ/mol	318.72	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[4.14e-05; 3759.58]	kPa	[105.15; 318.69]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38199e+01
Coefficient B			-1.55710e+03
Coefficient C			-4.00300e+01
Temperature range, min.			105.15
Temperature range, max.			318.69
Pvap	4.14e-05	kPa	105.15	Calculated Property
Pvap	0.02	kPa	128.88	Calculated Property
Pvap	0.99	kPa	152.60	Calculated Property
Pvap	10.98	kPa	176.33	Calculated Property
Pvap	59.72	kPa	200.06	Calculated Property
Pvap	209.77	kPa	223.78	Calculated Property
Pvap	552.83	kPa	247.51	Calculated Property
Pvap	1194.17	kPa	271.24	Calculated Property
Pvap	2235.02	kPa	294.96	Calculated Property
Pvap	3759.58	kPa	318.69	Calculated Property
Pvap	[162.63; 3757.65]	kPa	[215.15; 318.69]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			-2.45168e+01
Coefficient B			-1.02837e+03
Coefficient C			6.55630e+00
Coefficient D			-1.78874e-05
Coefficient E			2.00000e+00
Temperature range, min.			215.15
Temperature range, max.			318.69
Pvap	162.63	kPa	215.15	Calculated Property
Pvap	266.32	kPa	226.65	Calculated Property
Pvap	416.89	kPa	238.16	Calculated Property
Pvap	626.85	kPa	249.66	Calculated Property
Pvap	909.04	kPa	261.17	Calculated Property
Pvap	1275.76	kPa	272.67	Calculated Property
Pvap	1737.72	kPa	284.18	Calculated Property
Pvap	2303.05	kPa	295.68	Calculated Property
Pvap	2976.32	kPa	307.19	Calculated Property
Pvap	3757.65	kPa	318.69	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1849.93; 719.39]	kg/m3	[223.15; 318.72]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			1.46289e+02
Coefficient B			2.34350e-01
Coefficient C			3.18740e+02
Coefficient D			2.40270e-01
Comment			Range stopped at Tc; ChemSep gives it to 318.73 K.
Temperature range, min.			223.15
Temperature range, max.			318.72
ρl	1849.93	kg/m3	223.15	Calculated Property
ρl	1794.71	kg/m3	233.77	Calculated Property
ρl	1735.87	kg/m3	244.39	Calculated Property
ρl	1672.52	kg/m3	255.01	Calculated Property
ρl	1603.36	kg/m3	265.63	Calculated Property
ρl	1526.35	kg/m3	276.24	Calculated Property
ρl	1437.92	kg/m3	286.86	Calculated Property
ρl	1330.82	kg/m3	297.48	Calculated Property
ρl	1185.07	kg/m3	308.10	Calculated Property
ρl	719.39	kg/m3	318.72	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.01; 0.01]	N/m	[205.00; 253.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.87550e-02
Coefficient B			-1.84080e+02
Coefficient C			-6.23280e-01
Coefficient D			-1.06780e-02
Coefficient E			6.76590e-06
Temperature range, min.			205.00
Temperature range, max.			253.15
γ	0.01	N/m	205.00	Calculated Property
γ	0.01	N/m	210.35	Calculated Property
γ	0.01	N/m	215.70	Calculated Property
γ	0.01	N/m	221.05	Calculated Property
γ	0.01	N/m	226.40	Calculated Property
γ	0.01	N/m	231.75	Calculated Property
γ	0.01	N/m	237.10	Calculated Property
γ	0.01	N/m	242.45	Calculated Property
γ	0.01	N/m	247.80	Calculated Property
γ	0.01	N/m	253.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.05]	W/m×K	[223.15; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.32690e-03
Coefficient B			5.27270e-01
Coefficient C			3.02640e+01
Coefficient D			7.39300e+04
Temperature range, min.			223.15
Temperature range, max.			1000.00
λgas	0.01	W/m×K	223.15	Calculated Property
λgas	0.01	W/m×K	309.47	Calculated Property
λgas	0.02	W/m×K	395.78	Calculated Property
λgas	0.02	W/m×K	482.10	Calculated Property
λgas	0.03	W/m×K	568.42	Calculated Property
λgas	0.03	W/m×K	654.73	Calculated Property
λgas	0.04	W/m×K	741.05	Calculated Property
λgas	0.04	W/m×K	827.37	Calculated Property
λgas	0.04	W/m×K	913.68	Calculated Property
λgas	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.11; 0.04]	W/m×K	[223.15; 318.69]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-6.43310e-02
Coefficient B			-1.79320e+02
Coefficient C			3.69690e-01
Coefficient D			-5.06830e-03
Coefficient E			-4.06930e-06
Temperature range, min.			223.15
Temperature range, max.			318.69
λliquid	0.11	W/m×K	223.15	Calculated Property
λliquid	0.10	W/m×K	233.77	Calculated Property
λliquid	0.09	W/m×K	244.38	Calculated Property
λliquid	0.09	W/m×K	255.00	Calculated Property
λliquid	0.08	W/m×K	265.61	Calculated Property
λliquid	0.07	W/m×K	276.23	Calculated Property
λliquid	0.07	W/m×K	286.84	Calculated Property
λliquid	0.06	W/m×K	297.46	Calculated Property
λliquid	0.05	W/m×K	308.07	Calculated Property
λliquid	0.04	W/m×K	318.69	Calculated Property

Similar Compounds

Find more compounds similar to Sulfur hexafluoride.

Mixtures

• 2-PROPANOL, 1,1,1,3,3,3-HEXAFLUORO- + Sulfur hexafluoride + Water
• Furan, tetrahydro-2,5-dimethyl- + Furan, tetrahydro-2,5-dimethyl-, cis- + Sulfur hexafluoride
• Ethanol, 2,2,2-trifluoro- + Sulfur hexafluoride + Water
• 2,5,8,11-Tetraoxadodecane + Sulfur hexafluoride
• 2,5,8,11,14-Pentaoxapentadecane + Sulfur hexafluoride
• Carbonic acid, dimethyl ester + Sulfur hexafluoride
• Diethyl carbonate + Sulfur hexafluoride
• Tristearin + Sulfur hexafluoride
• Triolein + Sulfur hexafluoride

Sources

• Air Liquide Gas Encyclopedia
• 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).
• Mathews (1972), critical constants of inorganic substances ChEDL chemicals 1.5.2, from Mathews, J. F. Critical Constants of Inorganic Substances. Chem. Rev. 1972, 72, 71-100.
• 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.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Solubilities of several non-polar gases in mixtures water + 2,2,2-trifluoroethanol at 298.15 K and 101.33 kPa
• Kinematic viscosity and speed of sound in gaseous CO, CO2, SiF4, SF6, C4F8, and NH3 from 220 K to 375 K and pressures up to 3.4 MPa
• 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
• Viscosity Measurements on Gaseous Sulphur Hexafluoride
• Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
• Phase Equilibria of Glycerol Tristearate and Glycerol Trioleate in Carbon Dioxide and Sulfur Hexafluoride
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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