Chemical Properties of Propane, 2-(ethenyloxy)- (CAS 926-65-8)

InChI

InChI=1S/C5H10O/c1-4-6-5(2)3/h4-5H,1H2,2-3H3

InChI Key

GNUGVECARVKIPH-UHFFFAOYSA-N

Formula

C5H10O

SMILES

C=COC(C)C

Molecular Weight¹

86.13

CAS

926-65-8

Other Names

• 1-Isopropoxyethylene
• 2-(Ethenyloxy)propane
• 2-(vinyloxy)propane
• CH2=CHOCH(CH3)2
• Ether, isopropyl vinyl
• Isopropoxyethene
• Isopropoxyethylene
• Isopropyl vinyl ether
• Vinyl isopropyl ether

• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• 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).
• 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_vap : Vapor pressure (kPa).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔcH°liquid	[-3192.00; -3181.00]	kJ/mol
ΔcH°liquid	-3192.00 ± 0.80	kJ/mol	NIST
ΔcH°liquid	-3181.00 ± 8.80	kJ/mol	NIST
ΔfG°	-28.38	kJ/mol	Joback Calculated Property
ΔfH°gas	-174.00 ± 2.20	kJ/mol	NIST
ΔfH°liquid	-205.00 ± 0.80	kJ/mol	NIST
ΔfusH°	5.09	kJ/mol	Joback Calculated Property
ΔvapH°	31.00 ± 2.00	kJ/mol	NIST
IE	8.90	eV	NIST
log10WS	-1.46		Crippen Calculated Property
logPoct/wat	1.555		Crippen Calculated Property
McVol	82.880	ml/mol	McGowan Calculated Property
Pc	3607.21	kPa	Joback Calculated Property
Tboil	332.46	K	Joback Calculated Property
Tc	504.28	K	Joback Calculated Property
Tfus	151.58	K	Joback Calculated Property
Vc	0.308	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[135.00; 181.47]	J/mol×K	[332.46; 504.28]
Cp,gas	135.00	J/mol×K	332.46	Joback Calculated Property
Cp,gas	143.36	J/mol×K	361.10	Joback Calculated Property
Cp,gas	151.48	J/mol×K	389.73	Joback Calculated Property
Cp,gas	159.34	J/mol×K	418.37	Joback Calculated Property
Cp,gas	166.96	J/mol×K	447.01	Joback Calculated Property
Cp,gas	174.33	J/mol×K	475.64	Joback Calculated Property
Cp,gas	181.47	J/mol×K	504.28	Joback Calculated Property
η	[0.0001976; 0.0045847]	Pa×s	[151.58; 332.46]
η	0.0045847	Pa×s	151.58	Joback Calculated Property
η	0.0017577	Pa×s	181.73	Joback Calculated Property
η	0.0008853	Pa×s	211.87	Joback Calculated Property
η	0.0005290	Pa×s	242.02	Joback Calculated Property
η	0.0003542	Pa×s	272.17	Joback Calculated Property
η	0.0002570	Pa×s	302.31	Joback Calculated Property
η	0.0001976	Pa×s	332.46	Joback Calculated Property

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.62]	kPa	[243.92; 366.80]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.39543e+01
Coefficient B			-2.88922e+03
Coefficient C			-3.25150e+01
Temperature range, min.			243.92
Temperature range, max.			366.80
Pvap	1.33	kPa	243.92	Calculated Property
Pvap	3.05	kPa	257.57	Calculated Property
Pvap	6.37	kPa	271.23	Calculated Property
Pvap	12.25	kPa	284.88	Calculated Property
Pvap	22.05	kPa	298.53	Calculated Property
Pvap	37.47	kPa	312.19	Calculated Property
Pvap	60.61	kPa	325.84	Calculated Property
Pvap	93.93	kPa	339.49	Calculated Property
Pvap	140.23	kPa	353.15	Calculated Property
Pvap	202.62	kPa	366.80	Calculated Property

Similar Compounds

Find more compounds similar to Propane, 2-(ethenyloxy)-.

Sources

• Crippen Method
• Crippen Method
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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