Chemical Properties of 2-Heptadecanol (CAS 16813-18-6)

2-Heptadecanol

InChI
InChI=1S/C17H36O/c1-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17(2)18/h17-18H,3-16H2,1-2H3
InChI Key
ZNYQHFLBAPNPRC-UHFFFAOYSA-N
Formula
C17H36O
SMILES
CCCCCCCCCCCCCCCC(C)O
Molecular Weight1
256.47
CAS
16813-18-6
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Physical Properties

Property Value Unit Source
ω 0.9643 Relay (1.0) Calculated Property
ΔfG° -47.00 kJ/mol Joback Calculated Property
ΔfH°gas -582.52 kJ/mol Relay (1.0) Calculated Property
ΔfusH° 40.35 kJ/mol Joback Calculated Property
ΔvapH° 112.73 kJ/mol Relay (1.0) Calculated Property
IE 9.93 eV Relay (1.0) Calculated Property
log10WS -6.28 Relay (1.0) Calculated Property
logPoct/wat 5.848 Crippen Calculated Property
McVol 256.260 ml/mol McGowan Calculated Property
Pc 1322.31 kPa Joback Calculated Property
Inp [1909.00; 1909.00]   Show Hide
Inp 1909.00 NIST
Inp 1909.00 NIST
Tboil 581.25 K Relay (1.0) Calculated Property
Tc 754.77 K Relay (1.0) Calculated Property
Tfus 327.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Vc 1.018 m3/kmol Relay (1.0) Calculated Property

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [378.30; 915.58] 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-8.95600e+00
Coefficient B1.65874e+00
Coefficient C-9.34600e-04
Coefficient D2.00400e-07
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 378.30 J/mol×K 273.00 Calculated Property
Cp,gas 469.77 J/mol×K 353.78 Calculated Property
Cp,gas 551.82 J/mol×K 434.56 Calculated Property
Cp,gas 625.07 J/mol×K 515.33 Calculated Property
Cp,gas 690.18 J/mol×K 596.11 Calculated Property
Cp,gas 747.76 J/mol×K 676.89 Calculated Property
Cp,gas 798.46 J/mol×K 757.67 Calculated Property
Cp,gas 842.91 J/mol×K 838.44 Calculated Property
Cp,gas 881.74 J/mol×K 919.22 Calculated Property
Cp,gas 915.58 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0107242; 0.0000725] Pa×s [327.15; 590.12] 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 A-1.57490e+01
Coefficient B3.66857e+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.327.15
Temperature range, max.590.12
η 0.0107242 Pa×s 327.15 Calculated Property
η 0.0042762 Pa×s 356.37 Calculated Property
η 0.0019601 Pa×s 385.59 Calculated Property
η 0.0010028 Pa×s 414.81 Calculated Property
η 0.0005604 Pa×s 444.03 Calculated Property
η 0.0003365 Pa×s 473.25 Calculated Property
η 0.0002144 Pa×s 502.47 Calculated Property
η 0.0001435 Pa×s 531.69 Calculated Property
η 0.0001002 Pa×s 560.90 Calculated Property
η 0.0000725 Pa×s 590.12 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [467.92; 634.46] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.61609e+01
Coefficient B-5.70883e+03
Coefficient C-1.08270e+02
Temperature range, min.467.92
Temperature range, max.634.46
Pvap 1.33 kPa 467.92 Calculated Property
Pvap 2.90 kPa 486.42 Calculated Property
Pvap 5.86 kPa 504.93 Calculated Property
Pvap 11.13 kPa 523.43 Calculated Property
Pvap 20.02 kPa 541.94 Calculated Property
Pvap 34.31 kPa 560.44 Calculated Property
Pvap 56.37 kPa 578.95 Calculated Property
Pvap 89.18 kPa 597.45 Calculated Property
Pvap 136.46 kPa 615.96 Calculated Property
Pvap 202.66 kPa 634.46 Calculated Property

Similar Compounds

2-Undecanol. 2-Nonanol. 2-Nonadecanol. 2-Octanol, (R)-. 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-Heptadecanol.

Sources

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