Chemical Properties of 4,7-Methano-1H-indene, octahydro- (CAS 6004-38-2)

InChI

InChI=1S/C10H16/c1-2-9-7-4-5-8(6-7)10(9)3-1/h7-10H,1-6H2

InChI Key

LPSXSORODABQKT-UHFFFAOYSA-N

Formula

C10H16

SMILES

C1CC2C3CCC(C3)C2C1

Molecular Weight¹

136.23

CAS

6004-38-2

Other Names

• 2,3-Trimethylenenorbornane
• 4,7-Methanoindan, hexahydro-
• 4,7-methano-1H-indene, octahydro-, (3a.alpha.,4.alpha.,7.alpha.,7a.alpha.)-
• 4,7-methano-1H-indene, octahydro-, (3a.alpha.,4.beta.,7.beta.,7a.alpha.)-
• 4,7-methanoindan, hexahydro-, endo-
• 4,7-methanoindan, hexahydro-, exo-
• Bicyclo(2.2.1)heptane, 2,3-(1,3-propanediyl)-
• Hexadyro, 4,7-methaneindene
• Hexahydro-4,7-methanoindan
• JP-10
• NSC 22464
• Norbornane, 2,3-trimethylene-
• Octahydro-4,7-methano indene
• Octahydro-4,7-methano-1H-indene
• Tetrahydrocyclopentadiene dimer
• Tetrahydrodicyclopentadiene
• Tricyclo(5.2.1.0(2,6))decane
• Tricyclo[5.1.0-2.6]decane
• Tricyclo[5.2.1.0(sup2,6)]decane
• Trimethylenenorbornane
• endo-tetrahydrodicyclopentadiene
• endo-tricyclo[5.2.1.0(2,6)]decane
• exo-3,4,8,9-tetrahydrodicyclopentadiene
• exo-5,6-trimethylenenorbornane
• exo-octahydro-4,7-methano-1H-indene
• exo-tetrahydrobicyclopentadiene
• exo-tetrahydrodicyclopentadiene
• exo-tricyclo[5.2.1.02,6]decane
• exo-trimethylenenorbornane
• jp10
• tricyclo[5.2.1.02,6]decane

• Δ_cH°_solid : Standard solid 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).
• C_p,solid : Solid phase 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°_solid : Solid 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_subH° : Enthalpy of sublimation 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).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• γ : Surface Tension (N/m).
• 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°solid	[-6109.00; -6084.40]	kJ/mol
ΔcH°solid	-6109.00 ± 3.00	kJ/mol	NIST
ΔcH°solid	-6084.40	kJ/mol	NIST
ΔfG°	195.76	kJ/mol	Joback Calculated Property
ΔfH°gas	-60.20 ± 3.80	kJ/mol	NIST
ΔfH°solid	-113.10 ± 2.50	kJ/mol	NIST
ΔfusH°	15.03	kJ/mol	Joback Calculated Property
ΔsubH°	[52.90; 53.00]	kJ/mol
ΔsubH°	53.00 ± 1.00	kJ/mol	NIST
ΔsubH°	52.90	kJ/mol	NIST
ΔsubH°	52.90 ± 1.30	kJ/mol	NIST
ΔvapH°	37.46	kJ/mol	Joback Calculated Property
IE	9.30	eV	NIST
log10WS	-2.73		Crippen Calculated Property
logPoct/wat	2.833		Crippen Calculated Property
McVol	119.180	ml/mol	McGowan Calculated Property
Pc	3100.18	kPa	Joback Calculated Property
Inp	[1077.60; 1078.00]
Inp	1077.60		NIST
Inp	1078.00		NIST
I	[1243.00; 1243.40]
I	1243.40		NIST
I	1243.00		NIST
I	1243.40		NIST
Tboil	448.02	K	Joback Calculated Property
Tc	661.62	K	Joback Calculated Property
Tfus	352.00 ± 1.00	K	NIST
Vc	0.458	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[272.54; 378.92]	J/mol×K	[448.02; 661.62]
Cp,gas	272.54	J/mol×K	448.02	Joback Calculated Property
Cp,gas	293.60	J/mol×K	483.62	Joback Calculated Property
Cp,gas	313.20	J/mol×K	519.22	Joback Calculated Property
Cp,gas	331.44	J/mol×K	554.82	Joback Calculated Property
Cp,gas	348.41	J/mol×K	590.42	Joback Calculated Property
Cp,gas	364.21	J/mol×K	626.02	Joback Calculated Property
Cp,gas	378.92	J/mol×K	661.62	Joback Calculated Property
Cp,solid	241.40	J/mol×K	329.00	NIST
η	[0.0020936; 0.0030770]	Pa×s	[293.15; 313.15]
η	0.0030760	Pa×s	293.15	Densiti...
η	0.0030770	Pa×s	293.15	Densiti...
η	0.0030764	Pa×s	293.15	Densiti...
η	0.0027840	Pa×s	298.15	Densiti...
η	0.0027696	Pa×s	298.15	Densiti...
η	0.0025250	Pa×s	303.15	Densiti...
η	0.0025194	Pa×s	303.15	Densiti...
η	0.0021120	Pa×s	313.15	Densiti...
η	0.0020936	Pa×s	313.15	Densiti...
ΔfusH	[2.95; 3.07]	kJ/mol	[345.30; 352.00]
ΔfusH	3.07	kJ/mol	345.30	NIST
ΔfusH	2.95	kJ/mol	352.00	NIST
ΔfusH	2.95	kJ/mol	352.00	NIST
ΔfusH	2.95	kJ/mol	352.00	NIST
ΔvapH	[43.50; 46.00]	kJ/mol	[411.50; 425.50]
ΔvapH	43.50	kJ/mol	411.50	NIST
ΔvapH	46.00	kJ/mol	425.50	NIST
Pvap	[2.00; 101.60]	kPa	[344.02; 463.60]
Pvap	2.00	kPa	344.02	Vapor l...
Pvap	3.50	kPa	358.17	Vapor l...
Pvap	5.00	kPa	367.23	Vapor l...
Pvap	10.00	kPa	384.68	Vapor l...
Pvap	15.00	kPa	396.77	Vapor l...
Pvap	20.00	kPa	405.51	Vapor l...
Pvap	25.00	kPa	412.50	Vapor l...
Pvap	30.00	kPa	418.51	Vapor l...
Pvap	35.00	kPa	423.84	Vapor l...
Pvap	40.00	kPa	428.42	Vapor l...
Pvap	45.00	kPa	432.64	Vapor l...
Pvap	50.00	kPa	436.48	Vapor l...
Pvap	55.00	kPa	440.06	Vapor l...
Pvap	60.00	kPa	443.43	Vapor l...
Pvap	65.00	kPa	446.40	Vapor l...
Pvap	75.00	kPa	451.93	Vapor l...
Pvap	80.00	kPa	454.45	Vapor l...
Pvap	85.00	kPa	456.82	Vapor l...
Pvap	90.00	kPa	458.86	Vapor l...
Pvap	95.00	kPa	460.90	Vapor l...
Pvap	100.00	kPa	462.76	Vapor l...
Pvap	101.60	kPa	463.60	Vapor l...
ρl	[896.61; 935.88]	kg/m3	[293.15; 343.15]
ρl	935.85	kg/m3	293.15	Densiti...
ρl	935.88	kg/m3	293.15	Density...
ρl	932.00	kg/m3	298.15	Density...
ρl	931.95	kg/m3	298.15	Densiti...
ρl	928.06	kg/m3	303.15	Densiti...
ρl	928.08	kg/m3	303.15	Density...
ρl	924.16	kg/m3	308.15	Density...
ρl	924.17	kg/m3	308.15	Densiti...
ρl	920.26	kg/m3	313.15	Densiti...
ρl	920.24	kg/m3	313.15	Density...
ρl	916.31	kg/m3	318.15	Density...
ρl	916.33	kg/m3	318.15	Densiti...
ρl	912.38	kg/m3	323.15	Density...
ρl	912.40	kg/m3	323.15	Densiti...
ρl	908.46	kg/m3	328.15	Densiti...
ρl	908.44	kg/m3	328.15	Density...
ρl	904.50	kg/m3	333.15	Density...
ρl	904.52	kg/m3	333.15	Densiti...
ρl	900.56	kg/m3	338.15	Densiti...
ρl	896.61	kg/m3	343.15	Densiti...
ΔfusS	8.40	J/mol×K	352.00	NIST
γ	[0.03; 0.03]	N/m	[293.15; 303.15]
γ	0.03	N/m	293.15	Density...
γ	0.03	N/m	303.15	Density...

Datasets

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
323.34	100.00	219.49
323.37	1030.00	219.39
323.37	2050.00	218.99
323.35	3070.00	218.80
323.34	4000.00	218.30
323.34	5020.00	218.14
323.35	6080.00	217.34
333.20	100.00	224.40
333.20	1070.00	224.39
333.21	2020.00	224.41
333.20	3000.00	223.84
333.16	3990.00	223.29
333.17	5040.00	223.42
333.17	5990.00	223.32
343.01	100.00	230.29
343.03	1090.00	230.02
343.06	2070.00	229.60
343.06	3060.00	229.00
343.09	4000.00	229.50
343.09	5030.00	228.72
343.09	6000.00	229.08
353.59	100.00	234.98
353.61	1080.00	234.61
353.61	2010.00	234.35
353.62	3070.00	234.12
353.59	4080.00	234.11
353.59	5070.00	234.17
353.60	6090.00	233.83
363.48	100.00	240.37
363.53	1070.00	240.28
363.53	2030.00	240.09
363.53	2990.00	239.97
363.54	4080.00	239.88
363.54	5000.00	239.76
363.55	6020.00	239.67
383.60	100.00	249.31
383.60	1000.00	248.82
383.61	2020.00	248.80
383.58	3060.00	248.68
383.58	4010.00	248.49
383.59	5070.00	248.39
383.60	5990.00	248.35
403.36	100.00	260.34
403.36	1020.00	259.74
403.37	2060.00	259.23
403.38	3040.00	258.89
403.38	4010.00	257.41
403.39	5000.00	256.93
403.40	6070.00	256.62
423.21	100.00	271.95
423.20	1020.00	271.44
423.20	2050.00	270.28
423.20	3010.00	268.73
423.25	4020.00	267.73
423.26	4980.00	267.54
423.27	6000.00	266.96
443.15	240.00	284.80
443.14	1030.00	284.05
443.13	2050.00	283.43
443.11	3110.00	282.78
443.17	4060.00	282.05
443.19	5030.00	281.38
443.18	6050.00	280.75
463.17	230.00	301.77
463.18	1060.00	300.31
463.16	2040.00	298.88
463.20	3000.00	299.41
463.19	4070.00	297.53
463.21	5010.00	297.44
463.22	6020.00	296.56
483.42	470.00	321.27
483.39	1020.00	319.24
483.31	2050.00	316.76
483.32	3040.00	315.54
483.37	4030.00	315.19
483.38	5080.00	314.31
483.37	6060.00	314.11
503.30	480.00	338.70
503.28	1020.00	336.59
503.28	2040.00	334.35
503.28	3050.00	333.03
503.29	4090.00	330.60
503.29	5070.00	331.61
503.30	6000.00	331.50
523.47	500.00	355.43
523.45	1030.00	352.98
523.45	2060.00	350.70
523.44	3010.00	348.07
523.50	4000.00	346.42
523.49	5040.00	345.42
523.49	6180.00	344.08
Reference

Similar Compounds

Find more compounds similar to 4,7-Methano-1H-indene, octahydro-.

Mixtures

• Cyclopentanol + 4,7-Methano-1H-indene, octahydro-
• Adamantane, 1,3-dimethyl- + 4,7-Methano-1H-indene, octahydro-
• Cyclopentanol + Adamantane, 1,3-dimethyl- + 4,7-Methano-1H-indene, octahydro-
• Cyclohexane, (1-methylethyl)- + 4,7-Methano-1H-indene, octahydro-
• Dodecanoic acid, methyl ester + 4,7-Methano-1H-indene, octahydro-
• Cyclohexane, (1-methylethyl)- + Dodecanoic acid, methyl ester + 4,7-Methano-1H-indene, octahydro-
• Undecane + 4,7-Methano-1H-indene, octahydro-
• Tetradecane + 4,7-Methano-1H-indene, octahydro-
• Nonane + 4,7-Methano-1H-indene, octahydro-
• Dodecane + 4,7-Methano-1H-indene, octahydro-
• Tridecane + 4,7-Methano-1H-indene, octahydro-
• 1-Butanol + 4,7-Methano-1H-indene, octahydro-
• 1-Pentanol + 4,7-Methano-1H-indene, octahydro-

Sources

• Crippen Method
• Crippen Method
• Vapor liquid equilibrium, densities and viscosities for the binary system exo- and endo-tetrahydrodicyclopentadiene and pure component vapor pressures
• Isobaric heat capacities of exo-tetrahydrodicyclopentadiene at temperatures from 323 K to 523 K and pressures up to 6 MPa
• Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
• Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
• Densities and Viscosities of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with N-Undecane or N-Tetradecane at T = (293.15 to 313.15) K
• Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
• Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
• Joback Method
• McGowan Method
• NIST Webbook

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