Chemical Properties of 2-Octanol, (R)- (CAS 5978-70-1)

2-Octanol, (R)-

InChI
InChI=1S/C8H18O/c1-3-4-5-6-7-8(2)9/h8-9H,3-7H2,1-2H3/t8-/m0/s1
InChI Key
SJWFXCIHNDVPSH-QMMMGPOBSA-N
Formula
C8H18O
SMILES
CCCCCCC(C)O
Molecular Weight1
130.23
CAS
5978-70-1
Other Names
  • (R)-(-)-2-Octanol
  • l-octan-2-ol
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Physical Properties

Property Value Unit Source
ω 0.6471 Relay (1.0) Calculated Property
ΔfG° -122.78 kJ/mol Joback Calculated Property
ΔfH°gas -391.46 kJ/mol Relay (1.0) Calculated Property
ΔfusH° 17.04 kJ/mol Joback Calculated Property
ΔvapH° 68.94 kJ/mol Relay (1.0) Calculated Property
IE 9.81 eV Relay (1.0) Calculated Property
log10WS -2.11 Relay (1.0) Calculated Property
logPoct/wat 2.338 Crippen Calculated Property
McVol 129.450 ml/mol McGowan Calculated Property
Pc 2811.36 kPa Joback Calculated Property
Tboil [448.20; 449.65] K Show Hide
Tboil 448.20 K NIST
Tboil 449.65 ± 2.00 K NIST
Tc 625.01 K Relay (1.0) Calculated Property
Tfus 245.77 K Relay (1.0) Calculated Property
Vc 0.504 m3/kmol Relay (1.0) Calculated Property

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr 359.20 K 2.70 NIST

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [187.38; 451.27] 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-7.75000e-01
Coefficient B8.03740e-01
Coefficient C-4.45000e-04
Coefficient D9.33000e-08
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 187.38 J/mol×K 273.00 Calculated Property
Cp,gas 232.01 J/mol×K 353.78 Calculated Property
Cp,gas 272.12 J/mol×K 434.56 Calculated Property
Cp,gas 308.01 J/mol×K 515.33 Calculated Property
Cp,gas 339.98 J/mol×K 596.11 Calculated Property
Cp,gas 368.31 J/mol×K 676.89 Calculated Property
Cp,gas 393.32 J/mol×K 757.67 Calculated Property
Cp,gas 415.28 J/mol×K 838.44 Calculated Property
Cp,gas 434.50 J/mol×K 919.22 Calculated Property
Cp,gas 451.27 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.1178389; 0.0002454] Pa×s [225.74; 446.16] 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-1.46357e+01
Coefficient B2.82113e+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.225.74
Temperature range, max.446.16
η 0.1178389 Pa×s 225.74 Calculated Property
η 0.0346808 Pa×s 250.23 Calculated Property
η 0.0126940 Pa×s 274.72 Calculated Property
η 0.0054773 Pa×s 299.21 Calculated Property
η 0.0026839 Pa×s 323.70 Calculated Property
η 0.0014539 Pa×s 348.19 Calculated Property
η 0.0008537 Pa×s 372.68 Calculated Property
η 0.0005353 Pa×s 397.17 Calculated Property
η 0.0003543 Pa×s 421.66 Calculated Property
η 0.0002454 Pa×s 446.16 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [346.12; 471.87] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.65048e+01
Coefficient B-4.54366e+03
Coefficient C-6.59440e+01
Temperature range, min.346.12
Temperature range, max.471.87
Pvap 1.33 kPa 346.12 Calculated Property
Pvap 2.88 kPa 360.09 Calculated Property
Pvap 5.80 kPa 374.06 Calculated Property
Pvap 11.00 kPa 388.04 Calculated Property
Pvap 19.78 kPa 402.01 Calculated Property
Pvap 33.93 kPa 415.98 Calculated Property
Pvap 55.84 kPa 429.95 Calculated Property
Pvap 88.58 kPa 443.93 Calculated Property
Pvap 135.97 kPa 457.90 Calculated Property
Pvap 202.64 kPa 471.87 Calculated Property

Similar Compounds

2-Undecanol. 2-Heptadecanol. 2-Nonanol. 2-Nonadecanol. 2-Tridecanol. 2-Octanol, (S)-. 2-Tetradecanol. 2-Dodecanol. 2-Hexadecanol. 2-PENTADECANOL. 2-Octanol. 2-Decanol. 2-Eicosanol. 2-Heptanol. 2-Heptanol, (R)-.

Find more compounds similar to 2-Octanol, (R)-.

Sources

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