Chemical Properties of Endo-2-methylnorbornane (CAS 765-90-2)

InChI

InChI=1S/C8H14/c1-6-4-7-2-3-8(6)5-7/h6-8H,2-5H2,1H3/t6-,7?,8?/m0/s1

InChI Key

KWSARSUDWPZTFF-KKMMWDRVSA-N

Formula

C8H14

SMILES

CC1CC2CCC1C2

Molecular Weight¹

110.20

CAS

765-90-2

Other Names

• endo-2-Methylbicyclo[2.2.1]heptane

• 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).
• η : Dynamic viscosity (Pa×s).
• 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).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[175.90; 189.70]	J/mol×K	[280.00; 310.00]
Cp,liquid	175.90	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	180.50	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	184.30	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	184.30	J/mol×K	298.15	NIST
Cp,liquid	185.10	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	189.70	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH	1.62	kJ/mol	278.30	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[125.68; 399.97]	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			-1.04050e+02
Coefficient B			1.02952e+00
Coefficient C			-7.50000e-04
Coefficient D			2.24500e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	125.68	J/mol×K	273.00	Calculated Property
Cp,gas	176.24	J/mol×K	353.78	Calculated Property
Cp,gas	220.13	J/mol×K	434.56	Calculated Property
Cp,gas	258.04	J/mol×K	515.33	Calculated Property
Cp,gas	290.70	J/mol×K	596.11	Calculated Property
Cp,gas	318.81	J/mol×K	676.89	Calculated Property
Cp,gas	343.08	J/mol×K	757.67	Calculated Property
Cp,gas	364.23	J/mol×K	838.44	Calculated Property
Cp,gas	382.95	J/mol×K	919.22	Calculated Property
Cp,gas	399.97	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0004672; 0.0004698]	Pa×s	[208.04; 417.62]	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			-7.65770e+00
Coefficient B			-2.28000e+00
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.			208.04
Temperature range, max.			417.62
η	0.0004672	Pa×s	208.04	Calculated Property
η	0.0004678	Pa×s	231.33	Calculated Property
η	0.0004682	Pa×s	254.61	Calculated Property
η	0.0004685	Pa×s	277.90	Calculated Property
η	0.0004688	Pa×s	301.18	Calculated Property
η	0.0004691	Pa×s	324.47	Calculated Property
η	0.0004693	Pa×s	347.76	Calculated Property
η	0.0004695	Pa×s	371.04	Calculated Property
η	0.0004697	Pa×s	394.33	Calculated Property
η	0.0004698	Pa×s	417.62	Calculated Property

Similar Compounds

Find more compounds similar to Endo-2-methylnorbornane.

Sources

• Cheméo Relay (1.0)
• Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
• Crippen Method
• Crippen Method
• Joback Method
• McGowan Method
• NIST Webbook
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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