Chemical Properties of Tetracyclo[3.2.0.0(2,7).0(4,6)]heptane (CAS 278-06-8)

Tetracyclo[3.2.0.0(2,7).0(4,6)]heptane

InChI
InChI=1S/C7H8/c1-2-4-5(2)7-3(1)6(4)7/h2-7H,1H2
InChI Key
DGZUEIPKRRSMGK-UHFFFAOYSA-N
Formula
C7H8
SMILES
C1C2C3C2C2C1C32
Molecular Weight1
92.14
CAS
278-06-8
Other Names
  • Quadricyclane
  • Tetracyclo[2.2.1.0(2,6).0(3,5)]heptane
  • [2.2.1.02,6.03,5]Quadricycloheptane
  • tetracyclo[2.2.1.02,6.03,5]heptane
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Physical Properties

Property Value Unit Source
ΔcH°liquid [-4200.00; -4114.30] kJ/mol Show Hide
ΔcH°liquid -4200.00 ± 2.20 kJ/mol NIST
ΔcH°liquid -4114.30 ± 1.10 kJ/mol NIST
ΔfH°gas [253.30; 339.10] kJ/mol Show Hide
ΔfH°gas 336.00 kJ/mol NIST
ΔfH°gas 333.00 kJ/mol NIST
ΔfH°gas 339.10 ± 2.30 kJ/mol NIST
ΔfH°gas 325.00 ± 4.20 kJ/mol NIST
ΔfH°gas 253.30 ± 1.10 kJ/mol NIST
ΔfH°liquid [216.30; 302.10] kJ/mol Show Hide
ΔfH°liquid 302.10 ± 2.20 kJ/mol NIST
ΔfH°liquid 216.30 ± 1.10 kJ/mol NIST
ΔfusH° 19.07 kJ/mol Joback Calculated Property
ΔvapH° [37.00; 37.90] kJ/mol Show Hide
ΔvapH° 37.85 ± 0.44 kJ/mol NIST
ΔvapH° 37.90 ± 0.10 kJ/mol NIST
ΔvapH° 37.90 ± 0.10 kJ/mol NIST
ΔvapH° 37.00 ± 0.80 kJ/mol NIST
ΔvapH° 37.00 kJ/mol NIST
ΔvapH° 37.00 ± 0.80 kJ/mol NIST
ΔvapH° 37.00 ± 0.20 kJ/mol NIST
ΔvapH° 37.00 kJ/mol NIST
IE [7.80; 8.70] eV Show Hide
IE 7.80 eV NIST
IE 8.70 eV NIST
IE 8.33 eV NIST
logPoct/wat 1.128 Crippen Calculated Property
McVol 66.050 ml/mol McGowan Calculated Property

Cheméo can also estimate Normal Boiling Point Temperature, Normal melting (fusion) point, 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 [139.10; 157.60] J/mol×K [297.00; 298.15] Show Hide
Cp,liquid 139.10 J/mol×K 297.00 NIST
Cp,liquid 157.60 J/mol×K 298.15 NIST
ΔfusH [1.09; 7.20] kJ/mol [180.00; 228.00] Show Hide
ΔfusH 7.20 kJ/mol 180.00 NIST
ΔfusH 1.09 kJ/mol 228.00 NIST
ΔfusH 1.09 kJ/mol 228.00 NIST
ΔvapH 37.30 ± 0.80 kJ/mol 337.00 NIST
ΔfusS [4.80; 40.00] J/mol×K [180.00; 228.00] Show Hide
ΔfusS 40.00 J/mol×K 180.00 NIST
ΔfusS 4.80 J/mol×K 228.00 NIST

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr 381.20 K 98.70 NIST

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [89.20; 303.84] J/mol×K [273.00; 1000.00] Joback Predicted correlation Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,gas in J/mol×K, T in K
Coefficient A-1.66960e+02
Coefficient B1.26740e+00
Coefficient C-1.35900e-03
Coefficient D5.62400e-07
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 89.20 J/mol×K 273.00 Calculated Property
Cp,gas 136.23 J/mol×K 353.78 Calculated Property
Cp,gas 173.32 J/mol×K 434.56 Calculated Property
Cp,gas 202.23 J/mol×K 515.33 Calculated Property
Cp,gas 224.76 J/mol×K 596.11 Calculated Property
Cp,gas 242.68 J/mol×K 676.89 Calculated Property
Cp,gas 257.77 J/mol×K 757.67 Calculated Property
Cp,gas 271.81 J/mol×K 838.44 Calculated Property
Cp,gas 286.57 J/mol×K 919.22 Calculated Property
Cp,gas 303.84 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0000245; 0.0009336] Pa×s [249.53; 379.12] Joback Predicted correlation Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A2.93200e-02
Coefficient B-2.65603e+03
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentLiquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.249.53
Temperature range, max.379.12
η 0.0000245 Pa×s 249.53 Calculated Property
η 0.0000439 Pa×s 263.93 Calculated Property
η 0.0000738 Pa×s 278.33 Calculated Property
η 0.0001181 Pa×s 292.73 Calculated Property
η 0.0001807 Pa×s 307.13 Calculated Property
η 0.0002662 Pa×s 321.52 Calculated Property
η 0.0003792 Pa×s 335.92 Calculated Property
η 0.0005249 Pa×s 350.32 Calculated Property
η 0.0007080 Pa×s 364.72 Calculated Property
η 0.0009336 Pa×s 379.12 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [278.94; 404.44] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.47079e+01
Coefficient B-3.38474e+03
Coefficient C-4.42240e+01
Temperature range, min.278.94
Temperature range, max.404.44
Pvap 1.33 kPa 278.94 Calculated Property
Pvap 2.99 kPa 292.88 Calculated Property
Pvap 6.16 kPa 306.83 Calculated Property
Pvap 11.81 kPa 320.77 Calculated Property
Pvap 21.25 kPa 334.72 Calculated Property
Pvap 36.23 kPa 348.66 Calculated Property
Pvap 58.96 kPa 362.61 Calculated Property
Pvap 92.11 kPa 376.55 Calculated Property
Pvap 138.81 kPa 390.50 Calculated Property
Pvap 202.66 kPa 404.44 Calculated Property

Similar Compounds

Tetracyclo[5.2.1.02,6.03,5]decane,(1α,2α,3β,5β,6α,7α)-. Anti-tricyclo[4.1.0.0(2,4)]heptane. Tetracyclo[4.1.0.0(2,4).0(3,5)]heptane. Tricycloprop[cd,f,hi]indene,decahydro-,(1aα,1bα,1cβ,2aβ,2bα,2cα,2dα,2eα)-. Pentacyclo[6.3.1.0(2,7).0(3,5).0(9,11)]dodecane. Tricyclo[2.2.1.0(2,6)]heptane. Tetracyclo[6.2.1.0(2,7).o(3,5)]undecane. Tricyclo[3.2.1.02,4]octan-8-one,(1«alpha»,2«alpha»,4«alpha»,5«alpha»)-. Tricyclo[3.2.1.02,4]octan-8-one,exo-. Tricyclo[3.2.1.02,4]octane,(1«alpha»,2«beta»,4«beta»,5«alpha»)-. Tricyclo[3.2.1.02,4]octane,(1«alpha»,2«alpha»,4«alpha»,5«alpha»)-. Pentacyclo[6.3.1.13,6.02,7.09,11]tridecane. Tricyclo[4.1.0.0(2,7)]heptane. Tetracyclo[3.3.1.02,8.04,6]nonane. Tetracyclo[7.1.0.02,4.05,7]decane(1«alpha»,2«alpha»,4«beta»,5«alpha»,7«alpha»,9«alpha»)-.

Find more compounds similar to Tetracyclo[3.2.0.0(2,7).0(4,6)]heptane.

Sources

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