Chemical Properties of Ethyl-1-propenyl ether (CAS 928-55-2)

InChI

InChI=1S/C5H10O/c1-3-5-6-4-2/h3,5H,4H2,1-2H3

InChI Key

XDHOEHJVXXTEDV-UHFFFAOYSA-N

Formula

C5H10O

SMILES

CC=COCC

Molecular Weight¹

86.13

CAS

928-55-2

Other Names

• 1-Ethoxy-1-propene
• 1-Ethoxyprop-1-ene
• 1-Ethoxypropene
• 1-Propene, 1-ethoxy-
• C2H5OCH=CHCH3
• Ether, ethyl propenyl
• Ethyl propenyl ether
• Propenyl ethyl ether

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fH°_gas : 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).
• I_np : Non-polar retention indices.
• 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
ω	0.2929		Relay (1.0) Calculated Property
PAff	876.60	kJ/mol	NIST
BasG	847.70	kJ/mol	NIST
ΔfH°gas	-191.40	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	10.10	kJ/mol	Joback Calculated Property
ΔvapH°	30.28	kJ/mol	Relay (1.0) Calculated Property
IE	8.45	eV	Relay (1.0) Calculated Property
log10WS	-1.44		Relay (1.0) Calculated Property
logPoct/wat	1.556		Crippen Calculated Property
McVol	82.880	ml/mol	McGowan Calculated Property
Pc	3615.89	kPa	Joback Calculated Property
Inp	[706.00; 706.00]
Inp	706.00		NIST
Inp	706.00		NIST
Tboil	337.27	K	Relay (1.0) Calculated Property
Tc	515.37	K	Relay (1.0) Calculated Property
Tfus	199.16	K	Relay (1.0) Calculated Property
Vc	0.313	m3/kmol	Relay (1.0) Calculated Property

Cheméo can also estimate Standard Gibbs free energy of formation 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.

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[112.95; 265.20]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			9.66100e+00
Coefficient B			4.35640e-01
Coefficient C			-2.21000e-04
Coefficient D			4.09000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	112.95	J/mol×K	273.00	Calculated Property
Cp,gas	137.93	J/mol×K	353.78	Calculated Property
Cp,gas	160.59	J/mol×K	434.56	Calculated Property
Cp,gas	181.07	J/mol×K	515.33	Calculated Property
Cp,gas	199.48	J/mol×K	596.11	Calculated Property
Cp,gas	215.97	J/mol×K	676.89	Calculated Property
Cp,gas	230.65	J/mol×K	757.67	Calculated Property
Cp,gas	243.67	J/mol×K	838.44	Calculated Property
Cp,gas	255.14	J/mol×K	919.22	Calculated Property
Cp,gas	265.20	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0028355; 0.0001494]	Pa×s	[163.26; 359.85]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.12531e+01
Coefficient B			8.79570e+02
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			163.26
Temperature range, max.			359.85
η	0.0028355	Pa×s	163.26	Calculated Property
η	0.0015015	Pa×s	185.10	Calculated Property
η	0.0009093	Pa×s	206.95	Calculated Property
η	0.0006060	Pa×s	228.79	Calculated Property
η	0.0004335	Pa×s	250.63	Calculated Property
η	0.0003272	Pa×s	272.48	Calculated Property
η	0.0002575	Pa×s	294.32	Calculated Property
η	0.0002094	Pa×s	316.16	Calculated Property
η	0.0001750	Pa×s	338.01	Calculated Property
η	0.0001494	Pa×s	359.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[255.52; 362.59]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.55860e+01
Coefficient B			-3.34994e+03
Coefficient C			-3.65460e+01
Temperature range, min.			255.52
Temperature range, max.			362.59
Pvap	1.33	kPa	255.52	Calculated Property
Pvap	2.93	kPa	267.42	Calculated Property
Pvap	5.97	kPa	279.31	Calculated Property
Pvap	11.38	kPa	291.21	Calculated Property
Pvap	20.46	kPa	303.11	Calculated Property
Pvap	35.01	kPa	315.00	Calculated Property
Pvap	57.31	kPa	326.90	Calculated Property
Pvap	90.25	kPa	338.80	Calculated Property
Pvap	137.32	kPa	350.69	Calculated Property
Pvap	202.64	kPa	362.59	Calculated Property

Similar Compounds

Find more compounds similar to Ethyl-1-propenyl ether.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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