Chemical Properties of 1,2-Dihexylcyclopropene (CAS 35365-52-7)

InChI

InChI=1S/C15H28/c1-3-5-7-9-11-14-13-15(14)12-10-8-6-4-2/h3-13H2,1-2H3

InChI Key

OTAPPAKLMIEBOQ-UHFFFAOYSA-N

Formula

C15H28

SMILES

CCCCCCC1=C(CCCCCC)C1

Molecular Weight¹

208.38

CAS

35365-52-7

Other Names

• Cyclopropene, 1,2-dihexyl-

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid 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_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).
• 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

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[296.61; 728.89]	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			-3.05500e+01
Coefficient B			1.43124e+00
Coefficient C			-9.21000e-04
Coefficient D			2.49200e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	296.61	J/mol×K	273.00	Calculated Property
Cp,gas	371.55	J/mol×K	353.78	Calculated Property
Cp,gas	437.93	J/mol×K	434.56	Calculated Property
Cp,gas	496.53	J/mol×K	515.33	Calculated Property
Cp,gas	548.14	J/mol×K	596.11	Calculated Property
Cp,gas	593.54	J/mol×K	676.89	Calculated Property
Cp,gas	633.53	J/mol×K	757.67	Calculated Property
Cp,gas	668.90	J/mol×K	838.44	Calculated Property
Cp,gas	700.42	J/mol×K	919.22	Calculated Property
Cp,gas	728.89	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0020928; 0.0003993]	Pa×s	[306.79; 515.19]	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			-1.02646e+01
Coefficient B			1.25641e+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.			306.79
Temperature range, max.			515.19
η	0.0020928	Pa×s	306.79	Calculated Property
η	0.0015700	Pa×s	329.95	Calculated Property
η	0.0012231	Pa×s	353.10	Calculated Property
η	0.0009826	Pa×s	376.26	Calculated Property
η	0.0008096	Pa×s	399.41	Calculated Property
η	0.0006814	Pa×s	422.57	Calculated Property
η	0.0005839	Pa×s	445.72	Calculated Property
η	0.0005080	Pa×s	468.88	Calculated Property
η	0.0004478	Pa×s	492.03	Calculated Property
η	0.0003993	Pa×s	515.19	Calculated Property

Similar Compounds

Find more compounds similar to 1,2-Dihexylcyclopropene.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Joback Method
• McGowan Method
• NIST Webbook

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