Acetic acid ethenyl ester (CAS 108-05-4)

InChI

InChI=1S/C4H6O2/c1-3-6-4(2)5/h3H,1H2,2H3

InChI Key

XTXRWKRVRITETP-UHFFFAOYSA-N

Formula

C4H6O2

SMILES

C=COC(C)=O

Molecular Weight¹

86.09

CAS

108-05-4

Other Names

1-Acetoxyethylene
Acetate de vinyle
Acetic acid vinyl ester
Acetic acid, ethylene ether
Acetoxyethene
CH3CO2CH=CH2
Ethenyl acetate
Everflex 81L
NSC 8404
Octan winylu
Plyamul 40305-00
Unocal 76 Res 6206
Unocal 76 Res S-55
VAC
Vinile (acetato di)
Vinnapas A 50
Vinyl A monomer
Vinyl acetate h.q.
Vinyl acetate monomer
Vinyl ester of acetic acid
Vinylacetaat
Vinylacetat
Vinyle (acetate de)
Vinylester kyseliny octove
VyAc
Zeset T
acetic acid, vinyl ester
ethanoic acid, ethenyl ester
ethenyl ethanoate
vinyl acetate
vinyl ethanoate

ω : Acentric Factor.
PAff : Proton affinity (kJ/mol).
T_ig : Autoignition Temperature (K).
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).
μ : Dipole Moment (debye).
η : Dynamic viscosity (Pa×s).
LFL : Lower Flammability Limit (% in Air).
UFL : Upper Flammability Limit (% in Air).
T_flash,cc : Flash Point (Closed Cup Method) (K).
T_flash,oc : Flash Point (Open Cup Method) (K).
Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
R_g : Radius of Gyration.
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_fusH : Enthalpy of fusion 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).
logP_oct/wat : Octanol/Water partition coefficient.
McVol : McGowan's characteristic volume (ml/mol).
NFPA Fire : NFPA Fire Rating.
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).
n₀ : Refractive Index.
ρ_l : Liquid Density (kg/m³).
I_np : Non-polar retention indices.
I_p : 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.

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Physical Properties

Property	Value	Unit	Source
ω	[0.3400; 0.5294]
ω	0.3767		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5294		ChemSep v8.3 pure component data Compiled value
ω	0.3400		KDB
PAff	813.90	kJ/mol	NIST
T_ig	699.82	K	KDB
BasG	782.90	kJ/mol	NIST
Δ_cH°_liquid	-2086.00 ± 10.00	kJ/mol	NIST
μ	[1.70; 1.79]	debye
μ	1.79	debye	ChemSep v8.3 pure component data Compiled value
μ	1.70	debye	KDB
LFL	2.60	% in Air	KDB
UFL	13.40	% in Air	KDB
T_flash,cc	268.15	K	KDB
T_flash,oc	265.37	K	KDB
Δ_fG°	-228.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
R_g	3.0890		KDB
Δ_fH°_gas	[-316.00; -309.00]	kJ/mol
Δ_fH°_gas	-315.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_gas	-316.00	kJ/mol	KDB
Δ_fH°_gas	-313.60	kJ/mol	NIST
Δ_fH°_gas	-309.00 ± 10.00	kJ/mol	NIST
Δ_fH°_liquid	[-350.80; -346.00]	kJ/mol
Δ_fH°_liquid	-350.80	kJ/mol	NIST
Δ_fH°_liquid	-346.00 ± 10.00	kJ/mol	NIST
Δ_fusH°	9.21	kJ/mol	Joback Calculated Property
Δ_vapH°	37.20 ± 0.84	kJ/mol	NIST
IE	[9.19; 9.85]	eV
IE	9.20	eV	NIST
IE	9.20	eV	NIST
IE	9.19 ± 0.05	eV	NIST
IE	9.85	eV	NIST
IE	9.85 ± 0.05	eV	NIST
logP_oct/wat	0.693		Crippen Calculated Property
McVol	70.360	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
NFPA Safety	2		KDB
P_c	[4150.00; 4350.00]	kPa
P_c	4185.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
P_c	4185.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
P_c	4150.00	kPa	ChemSep v8.3 pure component data Compiled value
P_c	4350.00	kPa	KDB
P_c	4185.00 ± 9.00	kPa	NIST
P_triple	7.06e-04	kPa	ChemSep v8.3 pure component data Compiled value
I_np	[524.00; 570.00]
I_np	564.00		NIST
I_np	527.00		NIST
I_np	529.00		NIST
I_np	545.00		NIST
I_np	548.00		NIST
I_np	524.00		NIST
I_np	546.00		NIST
I_np	551.00		NIST
I_np	570.00		NIST
I_np	570.00		NIST
I_np	560.00		NIST
I_np	562.00		NIST
I_np	562.00		NIST
I_np	562.00		NIST
I_np	548.00		NIST
I_np	564.00		NIST
I_p	[878.00; 878.00]
I_p	878.00		NIST
I_p	878.00		NIST
T_boil	[345.00; 346.15]	K
T_boil	346.10	K	Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
T_boil	345.75	K	Vapor Liquid Equilibrium at p/kPa = 101.3 of the Binary Mixtures of Ethenyl Acetate with Methanol and Butan-1-ol
T_boil	345.95	K	Isobaric Vapor Liquid Equilibrium of Binary Mixtures of Vinyl Acetate and Ethyl Formate with Cumene at 97.3 kPa
T_boil	345.65	K	ChemSep v8.3 pure component data Compiled value
T_boil	346.00	K	KDB
T_boil	345.71 ± 0.30	K	NIST
T_boil	345.71 ± 0.30	K	NIST
T_boil	345.50	K	NIST
T_boil	345.71 ± 0.30	K	NIST
T_boil	345.71 ± 0.30	K	NIST
T_boil	Outlier 345.00	K	NIST
T_boil	346.01 ± 0.40	K	NIST
T_boil	346.05	K	NIST
T_boil	345.65 ± 0.30	K	NIST
T_boil	346.15 ± 1.50	K	NIST
T_c	[501.45; 525.00]	K
T_c	519.20	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
T_c	519.13	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
T_c	501.45	K	ChemSep v8.3 pure component data Compiled value
T_c	525.00	K	KDB
T_c	519.13 ± 0.40	K	NIST
T_fus	[172.95; 180.35]	K
T_fus	176.55	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
T_fus	180.35	K	ChemSep v8.3 pure component data Compiled value
T_fus	173.00	K	KDB
T_fus	180.35	K	NIST
T_fus	172.95 ± 0.30	K	NIST
T_triple	180.35	K	ChemSep v8.3 pure component data Compiled value
U_Qi	2.90		ChemSep v8.3 pure component data Compiled value
U_Ri	3.25		ChemSep v8.3 pure component data Compiled value
V_c	[0.265; 0.266]	m³/kmol
V_c	0.265	m³/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
V_c	0.266	m³/kmol	ChemSep v8.3 pure component data Compiled value
V_c	0.265	m³/kmol	KDB
Z_c	[0.2480000; 0.2640820]
Z_c	0.2480000		ChemSep v8.3 pure component data Compiled value
Z_c	0.2640820		KDB
Z_ra	[0.25; 0.26]
Z_ra	0.25		ChemSep v8.3 pure component data Compiled value
Z_ra	0.26		KDB

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	169.50	J/mol×K	298.00	NIST
Δ_fusH	[8.46; 8.46]	kJ/mol	[180.60; 180.60]
Δ_fusH	8.46	kJ/mol	180.60	NIST
Δ_fusH	8.46	kJ/mol	180.60	NIST
Δ_vapH	[31.40; 34.40]	kJ/mol	[320.00; 347.50]
Δ_vapH	34.40	kJ/mol	320.00	NIST
Δ_vapH	31.40	kJ/mol	347.50	NIST
P_vap	[97.30; 101.30]	kPa	[344.68; 346.10]
P_vap	97.30	kPa	344.68	Vapor-Liquid Equilibria and Excess Properties of the Binary System Vinyl Acetate + p-Xylene
P_vap	101.30	kPa	345.75	Vapor Liquid Equilibrium at p/kPa = 101.3 of the Binary Mixtures of Ethenyl Acetate with Methanol and Butan-1-ol
P_vap	101.30	kPa	346.10	Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
n₀	[1.39253; 1.39260]		[293.15; 298.15]
n₀	1.39260		293.15	Measurement and Modeling of Liquid Liquid Equilibrium for the Systems Vinyl Acetate + Acetic Acid/Ethanol + Water at 298.15 and 308.15 K
n₀	1.39253		298.15	Density, Refractive Index, Speed of Sound, and Vapor-Liquid Equilibria for Binary Mixtures of Methanol + Vinyl Propionate and Vinyl Acetate + Vinyl Propionate. Vapor Pressures of Vinyl Propionate
ρ_l	[906.12; 932.00]	kg/m³	[293.00; 313.15]

ρ_l	932.00	kg/m³	293.00	KDB
ρ_l	931.95	kg/m³	293.15	Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρ_l	925.77	kg/m³	298.15	Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
ρ_l	925.77	kg/m³	298.15	Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
ρ_l	919.09	kg/m³	303.15	Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρ_l	919.40	kg/m³	303.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρ_l	913.13	kg/m³	308.15	Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
ρ_l	913.50	kg/m³	308.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρ_l	913.13	kg/m³	308.15	Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
ρ_l	906.12	kg/m³	313.15	Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρ_l	907.30	kg/m³	313.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[53.18; 236.69]	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 C_p,gas in J/mol×K, T in K
Coefficient A			5.06510e+01
Coefficient B			-4.32890e+02
Coefficient C			5.21024e+00
Coefficient D			4.87340e-04
Coefficient E			-1.89640e-07
Temperature range, min.			100.00
Temperature range, max.			1500.00

C_p,gas	53.18	J/mol×K	100.00	Calculated Property
C_p,gas	88.31	J/mol×K	255.56	Calculated Property
C_p,gas	126.26	J/mol×K	411.11	Calculated Property
C_p,gas	156.45	J/mol×K	566.67	Calculated Property
C_p,gas	180.18	J/mol×K	722.22	Calculated Property
C_p,gas	198.88	J/mol×K	877.78	Calculated Property
C_p,gas	213.43	J/mol×K	1033.33	Calculated Property
C_p,gas	224.38	J/mol×K	1188.89	Calculated Property
C_p,gas	232.05	J/mol×K	1344.44	Calculated Property
C_p,gas	236.69	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[139.80; 207.31]	J/mol×K	[213.41; 389.35]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is C_p,liquid in J/mol×K, T in K
Coefficient A			1.04670e+02
Coefficient B			6.82410e+01
Coefficient C			9.23145e-01
Coefficient D			1.30100e-02
Coefficient E			-1.01100e-05
Temperature range, min.			213.41
Temperature range, max.			389.35

C_p,liquid	139.80	J/mol×K	213.41	Calculated Property
C_p,liquid	145.04	J/mol×K	232.96	Calculated Property
C_p,liquid	150.91	J/mol×K	252.51	Calculated Property
C_p,liquid	157.40	J/mol×K	272.06	Calculated Property
C_p,liquid	164.49	J/mol×K	291.61	Calculated Property
C_p,liquid	172.15	J/mol×K	311.15	Calculated Property
C_p,liquid	180.33	J/mol×K	330.70	Calculated Property
C_p,liquid	188.98	J/mol×K	350.25	Calculated Property
C_p,liquid	198.01	J/mol×K	369.80	Calculated Property
C_p,liquid	207.31	J/mol×K	389.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0012369; 0.0001917]	Pa×s	[225.00; 401.00]	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			-2.01870e+01
Coefficient B			1.39800e+03
Coefficient C			1.33620e+00
Coefficient D			8.20760e-07
Coefficient E			2.00000e+00
Temperature range, min.			225.00
Temperature range, max.			401.00

η	0.0012369	Pa×s	225.00	Calculated Property
η	0.0008476	Pa×s	244.56	Calculated Property
η	0.0006203	Pa×s	264.11	Calculated Property
η	0.0004779	Pa×s	283.67	Calculated Property
η	0.0003838	Pa×s	303.22	Calculated Property
η	0.0003187	Pa×s	322.78	Calculated Property
η	0.0002721	Pa×s	342.33	Calculated Property
η	0.0002377	Pa×s	361.89	Calculated Property
η	0.0002117	Pa×s	381.44	Calculated Property
η	0.0001917	Pa×s	401.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Δ_vapH	[39.66; 2.78]	kJ/mol	[180.35; 501.30]	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 Δ_vapH in kJ/mol, T in K
Coefficient A			5.17841e+01
Coefficient B			1.32939e+00
Coefficient C			-3.12710e+00
Coefficient D			3.54290e+00
Coefficient E			-1.38480e+00
Critical temperature, Tc (K)			5.01450e+02
Temperature range, min.			180.35
Temperature range, max.			501.30

Δ_vapH	39.66	kJ/mol	180.35	Calculated Property
Δ_vapH	38.44	kJ/mol	216.01	Calculated Property
Δ_vapH	37.13	kJ/mol	251.67	Calculated Property
Δ_vapH	35.60	kJ/mol	287.33	Calculated Property
Δ_vapH	33.73	kJ/mol	322.99	Calculated Property
Δ_vapH	31.39	kJ/mol	358.66	Calculated Property
Δ_vapH	28.46	kJ/mol	394.32	Calculated Property
Δ_vapH	24.71	kJ/mol	429.98	Calculated Property
Δ_vapH	19.41	kJ/mol	465.64	Calculated Property
Δ_vapH	2.78	kJ/mol	501.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 3968.13]	kPa	[253.08; 519.13]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.48909e+01
Coefficient B			-3.20824e+03
Coefficient C			-3.33880e+01
Temperature range, min.			253.08
Temperature range, max.			519.13

P_vap	1.33	kPa	253.08	Calculated Property
P_vap	7.53	kPa	282.64	Calculated Property
P_vap	29.49	kPa	312.20	Calculated Property
P_vap	88.87	kPa	341.76	Calculated Property
P_vap	220.80	kPa	371.32	Calculated Property
P_vap	473.86	kPa	400.89	Calculated Property
P_vap	907.65	kPa	430.45	Calculated Property
P_vap	1588.80	kPa	460.01	Calculated Property
P_vap	2586.47	kPa	489.57	Calculated Property
P_vap	3968.13	kPa	519.13	Calculated Property
P_vap	[2.34e-03; 2963.26]	kPa	[180.35; 501.45]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is P_vap in kPa, T in K
Coefficient A			-3.58141e+01
Coefficient B			-2.45107e+03
Coefficient C			8.43748e+00
Coefficient D			-1.49690e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 519.13 K.
Temperature range, min.			180.35
Temperature range, max.			501.45

P_vap	2.34e-03	kPa	180.35	Calculated Property
P_vap	0.08	kPa	216.03	Calculated Property
P_vap	1.16	kPa	251.71	Calculated Property
P_vap	8.88	kPa	287.38	Calculated Property
P_vap	44.13	kPa	323.06	Calculated Property
P_vap	157.80	kPa	358.74	Calculated Property
P_vap	435.78	kPa	394.42	Calculated Property
P_vap	975.51	kPa	430.09	Calculated Property
P_vap	1832.51	kPa	465.77	Calculated Property
P_vap	2963.26	kPa	501.45	Calculated Property
P_vap	[9.50e-04; 4192.26]	kPa	[180.35; 524.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is P_vap in kPa, T in K
Coefficient A			4.86249e+01
Coefficient B			-5.47773e+03
Coefficient C			-4.86787e+00
Coefficient D			2.36709e-06
Coefficient E			0.00000e+00
Temperature range, min.			180.35
Temperature range, max.			524.00

P_vap	9.50e-04	kPa	180.35	Calculated Property
P_vap	0.08	kPa	218.53	Calculated Property
P_vap	1.55	kPa	256.72	Calculated Property
P_vap	13.12	kPa	294.90	Calculated Property
P_vap	64.55	kPa	333.08	Calculated Property
P_vap	220.12	kPa	371.27	Calculated Property
P_vap	580.62	kPa	409.45	Calculated Property
P_vap	1272.48	kPa	447.63	Calculated Property
P_vap	2431.86	kPa	485.82	Calculated Property
P_vap	4192.26	kPa	524.00	Calculated Property
P_vap	[83.96; 140.52]	kPa	[340.00; 355.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.66440e+01
Coefficient B			-4.16154e+03
Coefficient C			7.26000e-01
Reference			Swamy and Van Winkle, 1965
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			340.00
Temperature range, max.			355.00

P_vap	83.96	kPa	340.00	Calculated Property
P_vap	89.10	kPa	341.67	Calculated Property
P_vap	94.50	kPa	343.33	Calculated Property
P_vap	100.18	kPa	345.00	Calculated Property
P_vap	106.13	kPa	346.67	Calculated Property
P_vap	112.38	kPa	348.33	Calculated Property
P_vap	118.93	kPa	350.00	Calculated Property
P_vap	125.80	kPa	351.67	Calculated Property
P_vap	132.99	kPa	353.33	Calculated Property
P_vap	140.52	kPa	355.00	Calculated Property
P_vap	[13.15; 99.02]	kPa	[294.98; 345.19]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.45991e+01
Coefficient B			-2.99122e+03
Coefficient C			-4.61830e+01
Reference			Capková and Fried, 1963
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			294.98
Temperature range, max.			345.19

P_vap	13.15	kPa	294.98	Calculated Property
P_vap	17.12	kPa	300.56	Calculated Property
P_vap	22.03	kPa	306.14	Calculated Property
P_vap	28.06	kPa	311.72	Calculated Property
P_vap	35.38	kPa	317.30	Calculated Property
P_vap	44.19	kPa	322.87	Calculated Property
P_vap	54.71	kPa	328.45	Calculated Property
P_vap	67.19	kPa	334.03	Calculated Property
P_vap	81.87	kPa	339.61	Calculated Property
P_vap	99.02	kPa	345.19	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρ_l	[1056.64; 559.09]	kg/m³	[180.35; 501.45]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρ_l in kg/m³, T in K
Coefficient A			6.95920e+01
Coefficient B			2.38800e-01
Coefficient C			5.24340e+02
Coefficient D			2.51510e-01
Comment			Range stopped at Tc; ChemSep gives it to 524.33 K.
Temperature range, min.			180.35
Temperature range, max.			501.45

ρ_l	1056.64	kg/m³	180.35	Calculated Property
ρ_l	1020.30	kg/m³	216.03	Calculated Property
ρ_l	982.10	kg/m³	251.71	Calculated Property
ρ_l	941.60	kg/m³	287.38	Calculated Property
ρ_l	898.22	kg/m³	323.06	Calculated Property
ρ_l	851.09	kg/m³	358.74	Calculated Property
ρ_l	798.77	kg/m³	394.42	Calculated Property
ρ_l	738.67	kg/m³	430.09	Calculated Property
ρ_l	665.12	kg/m³	465.77	Calculated Property
ρ_l	559.09	kg/m³	501.45	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 1.44e-05]	N/m	[180.35; 501.30]	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			-4.49070e-03
Coefficient B			3.10640e+02
Coefficient C			-6.67280e+00
Coefficient D			1.48710e-02
Coefficient E			-2.70760e-05
Temperature range, min.			180.35
Temperature range, max.			501.30

γ	0.04	N/m	180.35	Calculated Property
γ	0.03	N/m	216.01	Calculated Property
γ	0.03	N/m	251.67	Calculated Property
γ	0.02	N/m	287.33	Calculated Property
γ	0.02	N/m	322.99	Calculated Property
γ	0.01	N/m	358.66	Calculated Property
γ	0.01	N/m	394.32	Calculated Property
γ	0.01	N/m	429.98	Calculated Property
γ	0.00	N/m	465.64	Calculated Property
γ	1.44e-05	N/m	501.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_gas	[0.00; 0.12]	W/m×K	[180.35; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ_gas in W/m×K, T in K
Coefficient A			-5.28190e+06
Coefficient B			-1.61540e-01
Coefficient C			2.84190e+09
Coefficient D			-1.70450e+13
Temperature range, min.			180.35
Temperature range, max.			1000.00

λ_gas	0.00	W/m×K	180.35	Calculated Property
λ_gas	0.01	W/m×K	271.42	Calculated Property
λ_gas	0.02	W/m×K	362.49	Calculated Property
λ_gas	0.03	W/m×K	453.57	Calculated Property
λ_gas	0.04	W/m×K	544.64	Calculated Property
λ_gas	0.05	W/m×K	635.71	Calculated Property
λ_gas	0.06	W/m×K	726.78	Calculated Property
λ_gas	0.08	W/m×K	817.86	Calculated Property
λ_gas	0.10	W/m×K	908.93	Calculated Property
λ_gas	0.12	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_liquid	[0.19; 0.11]	W/m×K	[180.35; 410.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ_liquid in W/m×K, T in K
Coefficient A			-6.81530e-02
Coefficient B			2.88480e+01
Coefficient C			-1.50160e+00
Coefficient D			5.13170e-04
Coefficient E			-3.00570e-06
Temperature range, min.			180.35
Temperature range, max.			410.00

λ_liquid	0.19	W/m×K	180.35	Calculated Property
λ_liquid	0.18	W/m×K	205.87	Calculated Property
λ_liquid	0.17	W/m×K	231.38	Calculated Property
λ_liquid	0.17	W/m×K	256.90	Calculated Property
λ_liquid	0.16	W/m×K	282.42	Calculated Property
λ_liquid	0.15	W/m×K	307.93	Calculated Property
λ_liquid	0.14	W/m×K	333.45	Calculated Property
λ_liquid	0.13	W/m×K	358.97	Calculated Property
λ_liquid	0.12	W/m×K	384.48	Calculated Property
λ_liquid	0.11	W/m×K	410.00	Calculated Property

Similar Compounds

Acetic acid, anhydride with formic acid.

Find more compounds similar to Acetic acid ethenyl ester.

Mixtures

Find more mixtures with Acetic acid ethenyl ester.

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.
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.
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
Phase equilibria of the ternary system vinyl acetate/(R,S)-1-phenylethanol/carbon dioxide at high pressure conditions
Activity coefficients and partial molar excess enthalpies at infinite dilution for four esters in water
Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
The study of excess molar volumes and related properties for binary mixtures containing benzyl alcohol and 1,3-dichloro-2-propanol with vinyl acetate, ethyl acetate and t-butyl acetate at T = 293.15 to 313.15 K and P = 0.087 MPa
Measurement and Modeling of Liquid Liquid Equilibrium for the Systems Vinyl Acetate + Acetic Acid/Ethanol + Water at 298.15 and 308.15 K
Bubble-Point Measurement for CO2 + Vinyl Acetate and CO2 + Vinyl Acrylate Systems at High Pressures.
Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
Density, Refractive Index, Speed of Sound, and Vapor-Liquid Equilibria for Binary Mixtures of Methanol + Vinyl Propionate and Vinyl Acetate + Vinyl Propionate. Vapor Pressures of Vinyl Propionate
Vapor-Liquid Equilibria and Excess Properties of the Binary System Vinyl Acetate + p-Xylene
Vapor Liquid Equilibrium at p/kPa = 101.3 of the Binary Mixtures of Ethenyl Acetate with Methanol and Butan-1-ol
Solubility of Flavonoids in Organic Solvents
Isobaric Vapor Liquid Equilibrium of Binary Mixtures of Vinyl Acetate and Ethyl Formate with Cumene at 97.3 kPa
Determination of Temperature-Dependent Henry s Law Constant of Four Oxygenated Solutes in Water Using Headspace Solid-Phase Microextraction Technique
Joback Method
KDB
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure

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