Chemical Properties of fluorine (CAS 7782-41-4)

InChI

InChI=1S/F2/c1-2

InChI Key

PXGOKWXKJXAPGV-UHFFFAOYSA-N

Formula

F2

SMILES

FF

Molecular Weight¹

38.00

CAS

7782-41-4

Other Names

• BIFLUORIDEN
• Fluorine molecule

• 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_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).
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety 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).
• S°_{gas,1 bar} : Molar entropy at standard conditions (1 bar) (J/mol×K).
• 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	[0.0510; 0.0588]
ω	0.0588		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.0510		ChemSep v8.3 pure component data Compiled value
ω	0.0540		KDB
PAff	332.00	kJ/mol	NIST
BasG	305.50	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
EA	[2.80; 3.17]	eV
EA	3.00 ± 0.07	eV	NIST
EA	3.12 ± 0.07	eV	NIST
EA	3.08	eV	NIST
EA	2.94 ± 0.20	eV	NIST
EA	2.90 ± 0.22	eV	NIST
EA	3.17	eV	NIST
EA	2.80 ± 0.30	eV	NIST
EA	3.08 ± 0.10	eV	NIST
EA	3.00	eV	NIST
ΔfG°	0.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[0.00; 0.00]	kJ/mol
ΔfH°gas	0.00	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	0.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	1.92	kJ/mol	Joback Calculated Property
IE	[15.69; 15.74]	eV
IE	15.70 ± 0.00	eV	NIST
IE	15.70 ± 0.00	eV	NIST
IE	15.70	eV	NIST
IE	15.69	eV	NIST
IE	15.70 ± 0.02	eV	NIST
IE	15.70 ± 0.01	eV	NIST
IE	15.70	eV	NIST
IE	Outlier 15.74	eV	NIST
IE	15.69 ± 0.01	eV	NIST
IE	15.70	eV	NIST
IE	15.69 ± 0.01	eV	NIST
IE	15.70	eV	NIST
IE	15.70	eV	NIST
logPoct/wat	0.840		Crippen Calculated Property
McVol	14.400	ml/mol	McGowan Calculated Property
NFPA Health	4		KDB
NFPA Safety	3		KDB
Pc	[5172.00; 5215.20]	kPa
Pc	5215.20	kPa	Mathews (1972), critical constants of inorganic substances Compiled value
Pc	5215.20	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5215.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5172.00	kPa	Air Liquide Gas Encyclopedia
Pc	5172.00	kPa	KDB
Ptriple	[0.24; 0.25]	kPa
Ptriple	0.25	kPa	Staveley, Lobo and Calado (1981), triple points Compiled value
Ptriple	0.25	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	0.24	kPa	Air Liquide Gas Encyclopedia
ρc	592.86	kg/m3	Air Liquide Gas Encyclopedia
S°gas,1 bar	202.79 ± 0.01	J/mol×K	NIST
Tboil	[84.95; 85.20]	K
Tboil	84.95	K	ChemSep v8.3 pure component data Compiled value
Tboil	85.04	K	Air Liquide Gas Encyclopedia
Tboil	85.03	K	KDB
Tboil	85.20 ± 0.30	K	NIST
Tc	[144.00; 144.41]	K
Tc	144.30	K	Mathews (1972), critical constants of inorganic substances Compiled value
Tc	144.31	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	144.30	K	ChemSep v8.3 pure component data Compiled value
Tc	144.41	K	Air Liquide Gas Encyclopedia
Tc	144.13	K	KDB
Tc	144.00 ± 1.00	K	NIST
Tfus	[53.49; 55.20]	K
Tfus	53.53	K	ChemSep v8.3 pure component data Compiled value
Tfus	53.54	K	Air Liquide Gas Encyclopedia
Tfus	53.49	K	KDB
Tfus	55.20 ± 0.30	K	NIST
Ttriple	[53.48; 53.48]	K
Ttriple	53.48	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	53.48	K	ChemSep v8.3 pure component data Compiled value
Ttriple	53.48	K	Air Liquide Gas Encyclopedia
UQi	0.88		ChemSep v8.3 pure component data Compiled value
URi	0.75		ChemSep v8.3 pure component data Compiled value
Vc	[0.066; 0.066]	m3/kmol
Vc	0.066	m3/kmol	Mathews (1972), critical constants of inorganic substances Compiled value
Vc	0.066	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.066	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.066	m3/kmol	KDB
Zc	[0.2848470; 0.2880000]
Zc	0.2880000		Mathews (1972), critical constants of inorganic substances Compiled value
Zc	0.2880000		ChemSep v8.3 pure component data Compiled value
Zc	0.2848470		KDB
Zra	[0.29; 0.29]
Zra	0.29		ChemSep v8.3 pure component data Compiled value
Zra	0.29		KDB

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	0.51	kJ/mol	53.54	Air Liquide Gas Encyclopedia
ΔvapH	6.63	kJ/mol	85.04	Air Liquide Gas Encyclopedia
ρg	[1.61; 5.64]	kg/m3	[85.04; 288.15]
ρg	5.64	kg/m3	85.04	Air Liquide Gas Encyclopedia
ρg	1.61	kg/m3	288.15	Air Liquide Gas Encyclopedia
ρl	[1501.78; 1510.00]	kg/m3	[85.00; 85.04]
ρl	1510.00	kg/m3	85.00	KDB
ρl	1501.78	kg/m3	85.04	Air Liquide Gas Encyclopedia

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[29.02; 38.23]	J/mol×K	[50.00; 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			2.90210e+01
Coefficient B			-7.21600e+02
Coefficient C			3.53239e+00
Coefficient D			-1.05401e-03
Coefficient E			3.33190e-07
Temperature range, min.			50.00
Temperature range, max.			1500.00
Cp,gas	29.02	J/mol×K	50.00	Calculated Property
Cp,gas	29.93	J/mol×K	211.11	Calculated Property
Cp,gas	32.50	J/mol×K	372.22	Calculated Property
Cp,gas	34.56	J/mol×K	533.33	Calculated Property
Cp,gas	35.86	J/mol×K	694.44	Calculated Property
Cp,gas	36.64	J/mol×K	855.56	Calculated Property
Cp,gas	37.15	J/mol×K	1016.67	Calculated Property
Cp,gas	37.52	J/mol×K	1177.78	Calculated Property
Cp,gas	37.86	J/mol×K	1338.89	Calculated Property
Cp,gas	38.23	J/mol×K	1500.00	Calculated Property
Cp,gas	[31.33; 28.99]	J/mol×K	[298.00; 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			3.14451e+01
Coefficient B			8.41383e+00
Coefficient C			-2.77885e+00
Coefficient D			2.18104e-01
Coefficient E			-2.11175e-01
Reference			Chase, 1998
Comment			F=-10.43260, G=237.2770, H=0.000000; Data last reviewed in June, 1982
Temperature range, min.			298.00
Temperature range, max.			6000.00
Cp,gas	31.33	J/mol×K	298.00	Calculated Property
Cp,gas	36.80	J/mol×K	931.56	Calculated Property
Cp,gas	38.56	J/mol×K	1565.11	Calculated Property
Cp,gas	38.79	J/mol×K	2198.67	Calculated Property
Cp,gas	37.91	J/mol×K	2832.22	Calculated Property
Cp,gas	36.29	J/mol×K	3465.78	Calculated Property
Cp,gas	34.25	J/mol×K	4099.33	Calculated Property
Cp,gas	32.13	J/mol×K	4732.89	Calculated Property
Cp,gas	30.27	J/mol×K	5366.44	Calculated Property
Cp,gas	28.99	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[56.03; 64.27]	J/mol×K	[53.48; 110.00]	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			5.60310e+01
Coefficient B			-8.38210e+03
Coefficient C			2.60582e+02
Coefficient D			-2.72280e+00
Coefficient E			9.68890e-03
Temperature range, min.			53.48
Temperature range, max.			110.00
Cp,liquid	56.03	J/mol×K	53.48	Calculated Property
Cp,liquid	56.03	J/mol×K	59.76	Calculated Property
Cp,liquid	56.05	J/mol×K	66.04	Calculated Property
Cp,liquid	56.24	J/mol×K	72.32	Calculated Property
Cp,liquid	56.84	J/mol×K	78.60	Calculated Property
Cp,liquid	57.72	J/mol×K	84.88	Calculated Property
Cp,liquid	58.59	J/mol×K	91.16	Calculated Property
Cp,liquid	59.49	J/mol×K	97.44	Calculated Property
Cp,liquid	60.94	J/mol×K	103.72	Calculated Property
Cp,liquid	64.27	J/mol×K	110.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0007323; 0.0000600]	Pa×s	[53.48; 140.00]	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			9.28950e+00
Coefficient B			-8.69030e+01
Coefficient C			-3.74450e+00
Coefficient D			5.84770e-06
Coefficient E			2.00000e+00
Temperature range, min.			53.48
Temperature range, max.			140.00
η	0.0007323	Pa×s	53.48	Calculated Property
η	0.0005085	Pa×s	63.09	Calculated Property
η	0.0003614	Pa×s	72.71	Calculated Property
η	0.0002633	Pa×s	82.32	Calculated Property
η	0.0001964	Pa×s	91.93	Calculated Property
η	0.0001496	Pa×s	101.55	Calculated Property
η	0.0001162	Pa×s	111.16	Calculated Property
η	0.0000918	Pa×s	120.77	Calculated Property
η	0.0000737	Pa×s	130.39	Calculated Property
η	0.0000600	Pa×s	140.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[7.64; 0.00]	kJ/mol	[53.48; 144.30]	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			2.74970e+01
Coefficient B			7.21120e+00
Coefficient C			-1.76990e+01
Coefficient D			1.78950e+01
Coefficient E			-6.77810e+00
Critical temperature, Tc (K)			1.44300e+02
Comment			Range stopped at Tc; ChemSep gives it to 144.41 K.
Temperature range, min.			53.48
Temperature range, max.			144.30
ΔvapH	7.64	kJ/mol	53.48	Calculated Property
ΔvapH	7.20	kJ/mol	63.57	Calculated Property
ΔvapH	6.89	kJ/mol	73.66	Calculated Property
ΔvapH	6.61	kJ/mol	83.75	Calculated Property
ΔvapH	6.28	kJ/mol	93.84	Calculated Property
ΔvapH	5.86	kJ/mol	103.94	Calculated Property
ΔvapH	5.29	kJ/mol	114.03	Calculated Property
ΔvapH	4.56	kJ/mol	124.12	Calculated Property
ΔvapH	3.49	kJ/mol	134.21	Calculated Property
ΔvapH	0.00	kJ/mol	144.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.25; 5229.44]	kPa	[53.48; 144.31]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38604e+01
Coefficient B			-7.37058e+02
Coefficient C			-5.20000e+00
Temperature range, min.			53.48
Temperature range, max.			144.31
Pvap	0.25	kPa	53.48	Calculated Property
Pvap	3.43	kPa	63.57	Calculated Property
Pvap	22.08	kPa	73.66	Calculated Property
Pvap	88.05	kPa	83.76	Calculated Property
Pvap	256.23	kPa	93.85	Calculated Property
Pvap	599.38	kPa	103.94	Calculated Property
Pvap	1197.62	kPa	114.03	Calculated Property
Pvap	2127.71	kPa	124.13	Calculated Property
Pvap	3455.08	kPa	134.22	Calculated Property
Pvap	5229.44	kPa	144.31	Calculated Property
Pvap	[0.27; 4928.93]	kPa	[53.45; 144.30]	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			1.22752e+01
Coefficient B			-8.40686e+02
Coefficient C			5.60464e-01
Coefficient D			-3.52006e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 144.41 K.
Temperature range, min.			53.45
Temperature range, max.			144.30
Pvap	0.27	kPa	53.45	Calculated Property
Pvap	3.42	kPa	63.54	Calculated Property
Pvap	21.71	kPa	73.64	Calculated Property
Pvap	87.35	kPa	83.73	Calculated Property
Pvap	257.44	kPa	93.83	Calculated Property
Pvap	606.74	kPa	103.92	Calculated Property
Pvap	1210.54	kPa	114.02	Calculated Property
Pvap	2124.85	kPa	124.11	Calculated Property
Pvap	3371.07	kPa	134.21	Calculated Property
Pvap	4928.93	kPa	144.30	Calculated Property
Pvap	[0.30; 5135.09]	kPa	[53.99; 143.99]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38697e+01
Coefficient B			-7.41587e+02
Coefficient C			-4.74800e+00
Reference			Straty and Prydz, 1970
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			53.99
Temperature range, max.			143.99
Pvap	0.30	kPa	53.99	Calculated Property
Pvap	3.86	kPa	63.99	Calculated Property
Pvap	23.56	kPa	73.99	Calculated Property
Pvap	91.03	kPa	83.99	Calculated Property
Pvap	259.80	kPa	93.99	Calculated Property
Pvap	600.18	kPa	103.99	Calculated Property
Pvap	1189.47	kPa	113.99	Calculated Property
Pvap	2101.83	kPa	123.99	Calculated Property
Pvap	3400.80	kPa	133.99	Calculated Property
Pvap	5135.09	kPa	143.99	Calculated Property
Pvap	[0.12; 103.69]	kPa	[50.00; 85.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.52504e+01
Coefficient B			-9.62391e+02
Coefficient C			5.41500e+00
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			50.00
Temperature range, max.			85.30
Pvap	0.12	kPa	50.00	Calculated Property
Pvap	0.38	kPa	53.92	Calculated Property
Pvap	1.04	kPa	57.84	Calculated Property
Pvap	2.52	kPa	61.77	Calculated Property
Pvap	5.56	kPa	65.69	Calculated Property
Pvap	11.28	kPa	69.61	Calculated Property
Pvap	21.33	kPa	73.53	Calculated Property
Pvap	37.98	kPa	77.46	Calculated Property
Pvap	64.20	kPa	81.38	Calculated Property
Pvap	103.69	kPa	85.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1663.59; 608.16]	kg/m3	[53.48; 144.30]	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			1.02603e+02
Coefficient B			2.31710e-01
Coefficient C			1.44420e+02
Coefficient D			2.15410e-01
Comment			Range stopped at Tc; ChemSep gives it to 144.41 K.
Temperature range, min.			53.48
Temperature range, max.			144.30
ρl	1663.59	kg/m3	53.48	Calculated Property
ρl	1609.41	kg/m3	63.57	Calculated Property
ρl	1551.67	kg/m3	73.66	Calculated Property
ρl	1489.52	kg/m3	83.75	Calculated Property
ρl	1421.67	kg/m3	93.84	Calculated Property
ρl	1346.13	kg/m3	103.94	Calculated Property
ρl	1259.41	kg/m3	114.03	Calculated Property
ρl	1154.46	kg/m3	124.12	Calculated Property
ρl	1011.84	kg/m3	134.21	Calculated Property
ρl	608.16	kg/m3	144.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.02; 6.62e-05]	N/m	[53.48; 144.12]	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			-2.39550e-03
Coefficient B			1.17160e+02
Coefficient C			-8.21100e+00
Coefficient D			6.39400e-02
Coefficient E			-3.76680e-04
Temperature range, min.			53.48
Temperature range, max.			144.12
γ	0.02	N/m	53.48	Calculated Property
γ	0.02	N/m	63.55	Calculated Property
γ	0.02	N/m	73.62	Calculated Property
γ	0.01	N/m	83.69	Calculated Property
γ	0.01	N/m	93.76	Calculated Property
γ	0.01	N/m	103.84	Calculated Property
γ	0.01	N/m	113.91	Calculated Property
γ	0.00	N/m	123.98	Calculated Property
γ	0.00	N/m	134.05	Calculated Property
γ	6.62e-05	N/m	144.12	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.06]	W/m×K	[70.00; 700.00]	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			1.26640e-04
Coefficient B			9.32290e-01
Coefficient C			1.66450e+00
Coefficient D			2.05530e+02
Temperature range, min.			70.00
Temperature range, max.			700.00
λgas	0.01	W/m×K	70.00	Calculated Property
λgas	0.01	W/m×K	140.00	Calculated Property
λgas	0.02	W/m×K	210.00	Calculated Property
λgas	0.02	W/m×K	280.00	Calculated Property
λgas	0.03	W/m×K	350.00	Calculated Property
λgas	0.04	W/m×K	420.00	Calculated Property
λgas	0.04	W/m×K	490.00	Calculated Property
λgas	0.05	W/m×K	560.00	Calculated Property
λgas	0.05	W/m×K	630.00	Calculated Property
λgas	0.06	W/m×K	700.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.21; 0.07]	W/m×K	[50.00; 130.00]	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			-1.54220e-01
Coefficient B			9.00030e+00
Coefficient C			-1.06080e+00
Coefficient D			-1.84870e-03
Coefficient E			-1.68200e-05
Temperature range, min.			50.00
Temperature range, max.			130.00
λliquid	0.21	W/m×K	50.00	Calculated Property
λliquid	0.19	W/m×K	58.89	Calculated Property
λliquid	0.17	W/m×K	67.78	Calculated Property
λliquid	0.15	W/m×K	76.67	Calculated Property
λliquid	0.14	W/m×K	85.56	Calculated Property
λliquid	0.12	W/m×K	94.44	Calculated Property
λliquid	0.11	W/m×K	103.33	Calculated Property
λliquid	0.09	W/m×K	112.22	Calculated Property
λliquid	0.08	W/m×K	121.11	Calculated Property
λliquid	0.07	W/m×K	130.00	Calculated Property

Similar Compounds

Find more compounds similar to fluorine.

Sources

• Air Liquide Gas Encyclopedia
• 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.
• 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
• Standard molar enthalpies of formation of copper(II) beta-diketonates and monothio-beta-diketonates
• Standard molar enthalpies of formation of nickel(II) I2-diketonates and monothio-I2-diketonates
• Experimental and computational thermochemical study of two fluorobenzazoles: 5-fluoro-2-methylbenzoxazole and 5-fluoro-2-methylbenzothiazole
• Isomorphism and phase diagram of Pb5(PO4)3F-Pb5(PO4)3Cl system
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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