Chemical Properties of 2-Decene, (E)- (CAS 20063-97-2)

InChI

InChI=1S/C10H20/c1-3-5-7-9-10-8-6-4-2/h3,5H,4,6-10H2,1-2H3/b5-3+

InChI Key

YKNMBTZOEVIJCM-HWKANZROSA-N

Formula

C10H20

SMILES

C/C=C/CCCCCCC

Molecular Weight¹

140.27

CAS

20063-97-2

Other Names

• (E)-2-C10H20
• (E)-2-Decene
• trans-2-Decene

• ω : Acentric Factor.
• 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_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_vap : Vapor pressure (kPa).
• I_np : Non-polar retention indices.
• I_p : 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	0.4339		Relay (1.0) Calculated Property
ΔfG°	113.54	kJ/mol	Joback Calculated Property
ΔfH°gas	-140.43	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	21.86	kJ/mol	Joback Calculated Property
ΔvapH°	51.14	kJ/mol	Relay (1.0) Calculated Property
IE	[8.90; 9.06]	eV
IE	8.90 ± 0.01	eV	NIST
IE	9.06 ± 0.01	eV	NIST
log10WS	-5.46		Relay (1.0) Calculated Property
logPoct/wat	3.923		Crippen Calculated Property
McVol	147.460	ml/mol	McGowan Calculated Property
Pc	2212.45	kPa	Joback Calculated Property
Inp	[990.00; 1009.00]
Inp	997.00		NIST
Inp	1004.00		NIST
Inp	1003.00		NIST
Inp	1002.00		NIST
Inp	1002.00		NIST
Inp	991.00		NIST
Inp	Outlier 990.00		NIST
Inp	1009.00		NIST
Inp	997.00		NIST
Inp	997.00		NIST
Inp	997.00		NIST
Inp	1003.00		NIST
Inp	1002.90		NIST
Inp	1003.10		NIST
Inp	996.60		NIST
Inp	996.70		NIST
Inp	1002.00		NIST
Inp	1005.00		NIST
Inp	1002.00		NIST
Inp	1003.00		NIST
Inp	997.00		NIST
Inp	Outlier 990.00		NIST
Inp	1002.00		NIST
Inp	997.00		NIST
Ip	[1060.00; 1066.30]
Ip	1065.00		NIST
Ip	1066.00		NIST
Ip	1066.00		NIST
Ip	1062.00		NIST
Ip	1064.00		NIST
Ip	1061.00		NIST
Ip	1061.00		NIST
Ip	1060.00		NIST
Ip	1065.30		NIST
Ip	1066.30		NIST
Ip	1062.00		NIST
Ip	1064.10		NIST
Ip	1065.30		NIST
Ip	1066.30		NIST
Ip	1062.00		NIST
Ip	1064.10		NIST
Ip	1062.00		NIST
Ip	1065.00		NIST
Ip	1061.00		NIST
Ip	1062.00		NIST
Ip	1064.10		NIST
Tboil	442.36	K	Relay (1.0) Calculated Property
Tc	617.30	K	Relay (1.0) Calculated Property
Tfus	211.05	K	Relay (1.0) Calculated Property
Vc	0.567	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[203.62; 504.66]	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			-2.03840e+01
Coefficient B			9.73840e-01
Coefficient C			-6.04000e-04
Coefficient D			1.55200e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	203.62	J/mol×K	273.00	Calculated Property
Cp,gas	255.42	J/mol×K	353.78	Calculated Property
Cp,gas	301.48	J/mol×K	434.56	Calculated Property
Cp,gas	342.30	J/mol×K	515.33	Calculated Property
Cp,gas	378.38	J/mol×K	596.11	Calculated Property
Cp,gas	410.19	J/mol×K	676.89	Calculated Property
Cp,gas	438.23	J/mol×K	757.67	Calculated Property
Cp,gas	463.00	J/mol×K	838.44	Calculated Property
Cp,gas	484.98	J/mol×K	919.22	Calculated Property
Cp,gas	504.66	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0057907; 0.0002110]	Pa×s	[197.38; 422.00]	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			-1.13744e+01
Coefficient B			1.22828e+03
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.			197.38
Temperature range, max.			422.00
η	0.0057907	Pa×s	197.38	Calculated Property
η	0.0028798	Pa×s	222.34	Calculated Property
η	0.0016490	Pa×s	247.30	Calculated Property
η	0.0010459	Pa×s	272.25	Calculated Property
η	0.0007161	Pa×s	297.21	Calculated Property
η	0.0005199	Pa×s	322.17	Calculated Property
η	0.0003952	Pa×s	347.13	Calculated Property
η	0.0003117	Pa×s	372.08	Calculated Property
η	0.0002533	Pa×s	397.04	Calculated Property
η	0.0002110	Pa×s	422.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.68]	kPa	[346.20; 461.20]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.74478e+01
Coefficient B			-4.76701e+03
Coefficient C			-6.84040e+01
Temperature range, min.			346.20
Temperature range, max.			461.20
Pvap	1.33	kPa	346.20	Calculated Property
Pvap	2.84	kPa	358.98	Calculated Property
Pvap	5.66	kPa	371.76	Calculated Property
Pvap	10.68	kPa	384.53	Calculated Property
Pvap	19.19	kPa	397.31	Calculated Property
Pvap	32.99	kPa	410.09	Calculated Property
Pvap	54.55	kPa	422.87	Calculated Property
Pvap	87.11	kPa	435.64	Calculated Property
Pvap	134.77	kPa	448.42	Calculated Property
Pvap	202.68	kPa	461.20	Calculated Property

Similar Compounds

Find more compounds similar to 2-Decene, (E)-.

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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