Chemical Properties of Acetic anhydride (CAS 108-24-7)

InChI

InChI=1S/C4H6O3/c1-3(5)7-4(2)6/h1-2H3

InChI Key

WFDIJRYMOXRFFG-UHFFFAOYSA-N

Formula

C4H6O3

SMILES

CC(=O)OC(C)=O

Molecular Weight¹

102.09

CAS

108-24-7

Other Names

• (CH3CO)2O
• Acetanhydride
• Acetic acid anhydride
• Acetic acid, 1,1'-anhydride
• Acetic acid, anhydride
• Acetic oxide
• Acetyl acetate
• Acetyl anhydride
• Acetyl ether
• Anhydrid kyseliny octove
• Anhydride acetique
• Anidride acetica
• Azijnzuuranhydride
• Essigsaeureanhydrid
• Ethanoic anhydrate
• Octowy bezwodnik
• UN 1715
• acetyl oxide
• ethanoic anhydride

• ω : Acentric Factor.
• 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (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).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (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	[0.4419; 0.8095]
ω	0.4419		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.8095		ChemSep v8.3 pure component data Compiled value
μ	2.79	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-476.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-573.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°liquid	-625.00 ± 3.40	kJ/mol	NIST
ΔfusH°	12.08	kJ/mol	Joback Calculated Property
ΔvapH°	38.75	kJ/mol	Relay (1.0) Calculated Property
IE	10.00	eV	NIST
log10WS	-0.10		Relay (1.0) Calculated Property
logPoct/wat	0.096		Crippen Calculated Property
McVol	76.230	ml/mol	McGowan Calculated Property
Pc	[4000.00; 4680.00]	kPa
Pc	4000.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	4000.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4280.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4000.00 ± 200.00	kPa	NIST
Pc	4680.00 ± 405.30	kPa	NIST
Ptriple	2.20e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[699.00; 706.00]
Inp	706.00		NIST
Inp	706.00		NIST
Inp	699.00		NIST
Inp	706.00		NIST
Ip	[1227.00; 1240.00]
Ip	1236.00		NIST
Ip	1240.00		NIST
Ip	1227.00		NIST
Ip	1227.00		NIST
S°gas	389.95	J/mol×K	NIST
Tboil	[403.55; 413.15]	K
Tboil	413.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	412.70	K	NIST
Tboil	412.70	K	NIST
Tboil	412.65 ± 0.40	K	NIST
Tboil	412.15 ± 1.00	K	NIST
Tboil	412.65 ± 0.50	K	NIST
Tboil	412.60 ± 0.50	K	NIST
Tboil	413.00 ± 0.40	K	NIST
Tboil	412.55 ± 1.00	K	NIST
Tboil	410.00 ± 3.00	K	NIST
Tboil	413.15 ± 0.30	K	NIST
Tboil	Outlier 403.55 ± 0.20	K	NIST
Tc	[569.00; 606.00]	K
Tc	606.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	606.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	569.15	K	ChemSep v8.3 pure component data Compiled value
Tc	606.00 ± 4.00	K	NIST
Tc	569.00 ± 20.00	K	NIST
Tfus	[199.02; 201.05]	K
Tfus	200.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	200.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	200.00	K	NIST
Tfus	200.15 ± 0.30	K	NIST
Tfus	199.05 ± 1.00	K	NIST
Tfus	199.02 ± 0.07	K	NIST
Tfus	199.11 ± 2.00	K	NIST
Tfus	200.15 ± 1.00	K	NIST
Tfus	201.05 ± 0.50	K	NIST
Tfus	200.15 ± 0.40	K	NIST
Tfus	200.05 ± 0.40	K	NIST
Ttriple	200.15	K	ChemSep v8.3 pure component data Compiled value
UQi	3.22		ChemSep v8.3 pure component data Compiled value
URi	3.59		ChemSep v8.3 pure component data Compiled value
Vc	[0.290; 0.290]	m3/kmol
Vc	0.290	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.290	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2300000		ChemSep v8.3 pure component data Compiled value
Zra	0.23		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[168.20; 204.34]	J/mol×K	[303.20; 333.15]
Cp,liquid	168.20	J/mol×K	303.20	NIST
Cp,liquid	200.73	J/mol×K	313.15	Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
Cp,liquid	204.34	J/mol×K	333.15	Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	[0.0005210; 0.0008880]	Pa×s	[293.15; 338.15]
η	0.0008880	Pa×s	293.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0008290	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0007780	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0007290	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0006880	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0006480	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0006100	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0005800	Pa×s	328.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0005480	Pa×s	333.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η	0.0005210	Pa×s	338.15	Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
ΔvapH	[43.30; 47.60]	kJ/mol	[366.50; 469.50]
ΔvapH	45.50	kJ/mol	366.50	NIST
ΔvapH	44.20	kJ/mol	374.00	NIST
ΔvapH	43.30	kJ/mol	389.00	NIST
ΔvapH	47.60	kJ/mol	469.50	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[317.00; 317.20]	K	[2.00; 2.00]
Tboilr	317.20	K	2.00	NIST
Tboilr	317.00	K	2.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[75.42; 257.27]	J/mol×K	[200.00; 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			6.38620e+01
Coefficient B			-7.16360e+02
Coefficient C			6.10824e+00
Coefficient D			-4.19440e-04
Coefficient E			1.17020e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	75.42	J/mol×K	200.00	Calculated Property
Cp,gas	113.16	J/mol×K	344.44	Calculated Property
Cp,gas	150.86	J/mol×K	488.89	Calculated Property
Cp,gas	180.43	J/mol×K	633.33	Calculated Property
Cp,gas	202.49	J/mol×K	777.78	Calculated Property
Cp,gas	218.98	J/mol×K	922.22	Calculated Property
Cp,gas	231.60	J/mol×K	1066.67	Calculated Property
Cp,gas	241.62	J/mol×K	1211.11	Calculated Property
Cp,gas	249.95	J/mol×K	1355.56	Calculated Property
Cp,gas	257.27	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[163.22; 235.71]	J/mol×K	[250.00; 413.15]	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			-7.60550e+01
Coefficient B			6.74260e+02
Coefficient C			-2.16626e+00
Coefficient D			2.68290e-02
Coefficient E			-2.81670e-05
Temperature range, min.			250.00
Temperature range, max.			413.15
Cp,liquid	163.22	J/mol×K	250.00	Calculated Property
Cp,liquid	172.84	J/mol×K	268.13	Calculated Property
Cp,liquid	184.05	J/mol×K	286.26	Calculated Property
Cp,liquid	195.88	J/mol×K	304.38	Calculated Property
Cp,liquid	207.47	J/mol×K	322.51	Calculated Property
Cp,liquid	218.01	J/mol×K	340.64	Calculated Property
Cp,liquid	226.72	J/mol×K	358.77	Calculated Property
Cp,liquid	232.94	J/mol×K	376.89	Calculated Property
Cp,liquid	236.08	J/mol×K	395.02	Calculated Property
Cp,liquid	235.71	J/mol×K	413.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0048338; 0.0002001]	Pa×s	[210.00; 469.00]	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			-1.31960e+01
Coefficient B			1.32130e+03
Coefficient C			2.91350e-01
Coefficient D			3.19380e-07
Coefficient E			2.00000e+00
Temperature range, min.			210.00
Temperature range, max.			469.00
η	0.0048338	Pa×s	210.00	Calculated Property
η	0.0023605	Pa×s	238.78	Calculated Property
η	0.0013519	Pa×s	267.56	Calculated Property
η	0.0008666	Pa×s	296.33	Calculated Property
η	0.0006034	Pa×s	325.11	Calculated Property
η	0.0004472	Pa×s	353.89	Calculated Property
η	0.0003479	Pa×s	382.67	Calculated Property
η	0.0002811	Pa×s	411.44	Calculated Property
η	0.0002342	Pa×s	440.22	Calculated Property
η	0.0002001	Pa×s	469.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[51.24; 19.81]	kJ/mol	[200.15; 563.28]	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			4.78756e+01
Coefficient B			-6.39261e-01
Coefficient C			1.65135e+00
Coefficient D			-7.78133e-01
Coefficient E			-4.11955e-02
Critical temperature, Tc (K)			5.69150e+02
Temperature range, min.			200.15
Temperature range, max.			563.28
ΔvapH	51.24	kJ/mol	200.15	Calculated Property
ΔvapH	50.12	kJ/mol	240.50	Calculated Property
ΔvapH	48.49	kJ/mol	280.85	Calculated Property
ΔvapH	46.41	kJ/mol	321.19	Calculated Property
ΔvapH	43.93	kJ/mol	361.54	Calculated Property
ΔvapH	41.12	kJ/mol	401.89	Calculated Property
ΔvapH	37.95	kJ/mol	442.24	Calculated Property
ΔvapH	34.34	kJ/mol	482.58	Calculated Property
ΔvapH	29.78	kJ/mol	522.93	Calculated Property
ΔvapH	19.81	kJ/mol	563.28	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[2.39e-05; 3936.26]	kPa	[200.15; 606.00]	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			8.78872e+01
Coefficient B			-8.62712e+03
Coefficient C			-1.04985e+01
Coefficient D			5.14480e-06
Coefficient E			2.00000e+00
Temperature range, min.			200.15
Temperature range, max.			606.00
Pvap	2.39e-05	kPa	200.15	Calculated Property
Pvap	8.68e-03	kPa	245.24	Calculated Property
Pvap	0.39	kPa	290.34	Calculated Property
Pvap	5.44	kPa	335.43	Calculated Property
Pvap	36.00	kPa	380.53	Calculated Property
Pvap	147.94	kPa	425.62	Calculated Property
Pvap	441.11	kPa	470.72	Calculated Property
Pvap	1053.64	kPa	515.81	Calculated Property
Pvap	2152.86	kPa	560.91	Calculated Property
Pvap	3936.26	kPa	606.00	Calculated Property
Pvap	[2.71e-05; 1447.59]	kPa	[200.15; 569.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.70607e+02
Coefficient B			-1.12828e+04
Coefficient C			-2.37023e+01
Coefficient D			2.12043e-05
Coefficient E			0.00000e+00
Temperature range, min.			200.15
Temperature range, max.			569.00
Pvap	2.71e-05	kPa	200.15	Calculated Property
Pvap	6.96e-03	kPa	241.13	Calculated Property
Pvap	0.24	kPa	282.12	Calculated Property
Pvap	2.58	kPa	323.10	Calculated Property
Pvap	14.10	kPa	364.08	Calculated Property
Pvap	50.47	kPa	405.07	Calculated Property
Pvap	139.20	kPa	446.05	Calculated Property
Pvap	327.62	kPa	487.03	Calculated Property
Pvap	704.19	kPa	528.02	Calculated Property
Pvap	1447.59	kPa	569.00	Calculated Property
Pvap	[5.94; 103.65]	kPa	[335.99; 412.57]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43832e+01
Coefficient B			-3.28756e+03
Coefficient C			-7.51130e+01
Reference			McDonald, Shrader, et al., 1959
Temperature range, min.			335.99
Temperature range, max.			412.57
Pvap	5.94	kPa	335.99	Calculated Property
Pvap	8.84	kPa	344.50	Calculated Property
Pvap	12.85	kPa	353.01	Calculated Property
Pvap	18.26	kPa	361.52	Calculated Property
Pvap	25.42	kPa	370.03	Calculated Property
Pvap	34.75	kPa	378.53	Calculated Property
Pvap	46.70	kPa	387.04	Calculated Property
Pvap	61.79	kPa	395.55	Calculated Property
Pvap	80.56	kPa	404.06	Calculated Property
Pvap	103.65	kPa	412.57	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1211.51; 456.15]	kg/m3	[200.15; 584.64]	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			1.38259e+02
Coefficient B			3.06200e-01
Coefficient C			5.84650e+02
Coefficient D			4.33340e-01
Temperature range, min.			200.15
Temperature range, max.			584.64
ρl	1211.51	kg/m3	200.15	Calculated Property
ρl	1153.45	kg/m3	242.87	Calculated Property
ρl	1094.20	kg/m3	285.59	Calculated Property
ρl	1033.38	kg/m3	328.31	Calculated Property
ρl	970.39	kg/m3	371.03	Calculated Property
ρl	904.32	kg/m3	413.76	Calculated Property
ρl	833.63	kg/m3	456.48	Calculated Property
ρl	755.21	kg/m3	499.20	Calculated Property
ρl	660.87	kg/m3	541.92	Calculated Property
ρl	456.15	kg/m3	584.64	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.02]	N/m	[200.15; 412.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			7.47443e-02
Coefficient B			-1.43600e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			200.15
Temperature range, max.			412.15
γ	0.05	N/m	200.15	Calculated Property
γ	0.04	N/m	223.71	Calculated Property
γ	0.04	N/m	247.26	Calculated Property
γ	0.04	N/m	270.82	Calculated Property
γ	0.03	N/m	294.37	Calculated Property
γ	0.03	N/m	317.93	Calculated Property
γ	0.03	N/m	341.48	Calculated Property
γ	0.02	N/m	365.04	Calculated Property
γ	0.02	N/m	388.59	Calculated Property
γ	0.02	N/m	412.15	Calculated Property
γ	[0.04; 5.94e-04]	N/m	[200.15; 563.28]	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			-1.27650e-03
Coefficient B			2.52130e+02
Coefficient C			-6.14990e+00
Coefficient D			1.46010e-02
Coefficient E			-2.77470e-05
Temperature range, min.			200.15
Temperature range, max.			563.28
γ	0.04	N/m	200.15	Calculated Property
γ	0.04	N/m	240.50	Calculated Property
γ	0.03	N/m	280.85	Calculated Property
γ	0.03	N/m	321.19	Calculated Property
γ	0.02	N/m	361.54	Calculated Property
γ	0.01	N/m	401.89	Calculated Property
γ	0.01	N/m	442.24	Calculated Property
γ	0.01	N/m	482.58	Calculated Property
γ	0.00	N/m	522.93	Calculated Property
γ	5.94e-04	N/m	563.28	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.07]	W/m×K	[200.15; 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			3.96700e-04
Coefficient B			8.13490e-01
Coefficient C			4.26600e+02
Coefficient D			1.40300e+05
Temperature range, min.			200.15
Temperature range, max.			1000.00
λgas	0.00	W/m×K	200.15	Calculated Property
λgas	0.01	W/m×K	289.02	Calculated Property
λgas	0.02	W/m×K	377.89	Calculated Property
λgas	0.02	W/m×K	466.77	Calculated Property
λgas	0.03	W/m×K	555.64	Calculated Property
λgas	0.04	W/m×K	644.51	Calculated Property
λgas	0.05	W/m×K	733.38	Calculated Property
λgas	0.05	W/m×K	822.26	Calculated Property
λgas	0.06	W/m×K	911.13	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.14]	W/m×K	[200.15; 412.70]	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			1.72360e-03
Coefficient B			-1.19780e+01
Coefficient C			-1.34130e+00
Coefficient D			-1.28230e-03
Coefficient E			-6.13880e-07
Temperature range, min.			200.15
Temperature range, max.			412.70
λliquid	0.19	W/m×K	200.15	Calculated Property
λliquid	0.18	W/m×K	223.77	Calculated Property
λliquid	0.18	W/m×K	247.38	Calculated Property
λliquid	0.17	W/m×K	271.00	Calculated Property
λliquid	0.16	W/m×K	294.62	Calculated Property
λliquid	0.16	W/m×K	318.23	Calculated Property
λliquid	0.15	W/m×K	341.85	Calculated Property
λliquid	0.15	W/m×K	365.47	Calculated Property
λliquid	0.14	W/m×K	389.08	Calculated Property
λliquid	0.14	W/m×K	412.70	Calculated Property

Similar Compounds

Find more compounds similar to Acetic anhydride.

Mixtures

• Acetic anhydride + Carbon dioxide
• Benzenemethanol, «alpha»-methyl- + Acetic anhydride + Carbon dioxide
• Acetic anhydride + Acetic acid
• Acetic anhydride + 2H-Pyran-2,6(3H)-dione, dihydro- + Carbon Tetrachloride
• Acetic anhydride + 2H-Pyran-2,6(3H)-dione, dihydro-
• Acetic anhydride + 2H-Pyran-2,6(3H)-dione, dihydro- + Acetic acid
• Acetic anhydride + Ethanol
• Acetic anhydride + Acetic acid + Ethyl Acetate
• Acetic anhydride + Ethanol + Acetic acid
• Acetic anhydride + Ethanol + Ethyl Acetate

Sources

• KDB Vapor Pressure Data
• 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 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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.
• Cheméo Relay (1.0)
• 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
• High pressure vapour liquid equilibria of the binary and some of the ternary and multicomponent mixtures of the carbon dioxide + acetic anhydride + alpha-methylbenzyl alcohol + acetic acid + alpha-methylbenzyl acetate system: Experimental and modelling results
• Measurement and correlation of solubility of D-camphor-10-sulfonic acid in pure solvents
• Solubility Determination and Thermodynamic Modeling of Glutaric Anhydride in Diverse Solvent Systems Consisting of Acetic Acid, Ethanoic Anhydride, and Tetrachloromethane from T = (278.45 to 324.45) K
• Evaluation of Excess Molar Enthalpies for a Quaternary Mixture System of Acetic Anhydride, Ethanol, Acetic Acid, and Ethyl Acetate
• Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
• Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
• Joback Method
• KDB
• McGowan Method
• NIST Webbook

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