Chemical Properties of 7-Methyloctan-1-ol (CAS 2430-22-0)

7-Methyloctan-1-ol

InChI
InChI=1S/C9H20O/c1-9(2)7-5-3-4-6-8-10/h9-10H,3-8H2,1-2H3
InChI Key
QDTDKYHPHANITQ-UHFFFAOYSA-N
Formula
C9H20O
SMILES
CC(C)CCCCCCO
Molecular Weight1
144.25
CAS
2430-22-0
Other Names
  • 1-Octanol, 7-methyl-
  • 7-methyl-1-octanol
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Physical Properties

Property Value Unit Source
ω 0.7118 Relay (1.0) Calculated Property
ΔfG° -114.36 kJ/mol Joback Calculated Property
ΔfH°gas -401.34 kJ/mol Relay (1.0) Calculated Property
ΔfusH° 19.63 kJ/mol Joback Calculated Property
ΔvapH° 74.08 kJ/mol Relay (1.0) Calculated Property
IE 9.83 eV Relay (1.0) Calculated Property
log10WS -3.04 Relay (1.0) Calculated Property
logPoct/wat 2.585 Crippen Calculated Property
McVol 143.540 ml/mol McGowan Calculated Property
Pc 2545.61 kPa Joback Calculated Property
Inp [1138.00; 1144.00]   Show Hide
Inp 1138.00 NIST
Inp 1140.00 NIST
Inp 1144.00 NIST
Inp 1144.00 NIST
Tboil 484.55 K Relay (1.0) Calculated Property
Tc 670.81 K Relay (1.0) Calculated Property
Tfus 337.65 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Vc 0.531 m3/kmol Relay (1.0) Calculated Property

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [208.59; 502.86] 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-1.68400e+00
Coefficient B8.98740e-01
Coefficient C-4.99400e-04
Coefficient D1.05200e-07
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 208.59 J/mol×K 273.00 Calculated Property
Cp,gas 258.42 J/mol×K 353.78 Calculated Property
Cp,gas 303.20 J/mol×K 434.56 Calculated Property
Cp,gas 343.24 J/mol×K 515.33 Calculated Property
Cp,gas 378.89 J/mol×K 596.11 Calculated Property
Cp,gas 410.48 J/mol×K 676.89 Calculated Property
Cp,gas 438.33 J/mol×K 757.67 Calculated Property
Cp,gas 462.79 J/mol×K 838.44 Calculated Property
Cp,gas 484.19 J/mol×K 919.22 Calculated Property
Cp,gas 502.86 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0022466; 0.0002212] Pa×s [337.65; 461.58] 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 A-1.47324e+01
Coefficient B2.91529e+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.337.65
Temperature range, max.461.58
η 0.0022466 Pa×s 337.65 Calculated Property
η 0.0016017 Pa×s 351.42 Calculated Property
η 0.0011715 Pa×s 365.19 Calculated Property
η 0.0008765 Pa×s 378.96 Calculated Property
η 0.0006693 Pa×s 392.73 Calculated Property
η 0.0005205 Pa×s 406.50 Calculated Property
η 0.0004115 Pa×s 420.27 Calculated Property
η 0.0003302 Pa×s 434.04 Calculated Property
η 0.0002686 Pa×s 447.81 Calculated Property
η 0.0002212 Pa×s 461.58 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [0.15; 202.64] kPa [337.65; 487.44] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.80069e+01
Coefficient B-5.24432e+03
Coefficient C-7.43540e+01
Temperature range, min.337.65
Temperature range, max.487.44
Pvap 0.15 kPa 337.65 Calculated Property
Pvap 0.48 kPa 354.29 Calculated Property
Pvap 1.38 kPa 370.94 Calculated Property
Pvap 3.54 kPa 387.58 Calculated Property
Pvap 8.24 kPa 404.22 Calculated Property
Pvap 17.68 kPa 420.87 Calculated Property
Pvap 35.37 kPa 437.51 Calculated Property
Pvap 66.60 kPa 454.15 Calculated Property
Pvap 118.92 kPa 470.80 Calculated Property
Pvap 202.64 kPa 487.44 Calculated Property

Similar Compounds

10-methylundecanol. Isoheptadecanol. 13-Methyltetradecan-1-ol. 1-Decanol, 9-methyl-. 12-Methyl-tridecanol. 1-Heptanol, 6-methyl-. 1-Hexanol, 5-methyl-. 6-Methyloctan-1-ol. 7-Methylnonan-1-ol. (S)-(+)-6-METHYL-1-OCTANOL. 5-Methyl-1-heptanol. 1-Nonanol, 4,8-dimethyl-. 4-Methyl-1-nonanol. 4-Methyl-1-undecanol. 4-Methyl-1-heptanol.

Find more compounds similar to 7-Methyloctan-1-ol.

Sources

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