Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -139.62 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -324.68 | kJ/mol | Joback Calculated Property |
ΔfusH° | 11.86 | kJ/mol | Joback Calculated Property |
ΔvapH° | 60.47 | kJ/mol | NIST |
log10WS | [-1.14; -1.14] | ||
log10WS | -1.14 | Aq. Sol... | |
log10WS | -1.14 | Estimat... | |
logPoct/wat | 1.415 | Crippen Calculated Property | |
McVol | 101.270 | ml/mol | McGowan Calculated Property |
Pc | 3484.76 | kPa | Joback Calculated Property |
Inp | [821.00; 875.00] | ||
Inp | 851.00 | NIST | |
Inp | 852.60 | NIST | |
Inp | 827.00 | NIST | |
Inp | 823.00 | NIST | |
Inp | 821.00 | NIST | |
Inp | Outlier 875.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 866.00 | NIST | |
Inp | 868.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 836.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 860.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 846.20 | NIST | |
Inp | 838.00 | NIST | |
Inp | 847.00 | NIST | |
Inp | 851.00 | NIST | |
Inp | 866.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 837.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 821.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 845.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 821.00 | NIST | |
Inp | 833.00 | NIST | |
Inp | 821.00 | NIST | |
Inp | Outlier 875.00 | NIST | |
Inp | 851.00 | NIST | |
Inp | 836.00 | NIST | |
Inp | 846.20 | NIST | |
Inp | 827.00 | NIST | |
Inp | 866.00 | NIST | |
I | [1282.00; 1347.00] | ||
I | 1338.00 | NIST | |
I | 1338.00 | NIST | |
I | 1300.00 | NIST | |
I | 1318.00 | NIST | |
I | 1320.00 | NIST | |
I | 1299.00 | NIST | |
I | 1312.00 | NIST | |
I | 1299.00 | NIST | |
I | 1311.00 | NIST | |
I | 1301.00 | NIST | |
I | 1301.00 | NIST | |
I | 1302.00 | NIST | |
I | 1301.00 | NIST | |
I | 1328.00 | NIST | |
I | Outlier 1347.00 | NIST | |
I | 1310.00 | NIST | |
I | 1309.00 | NIST | |
I | 1319.00 | NIST | |
I | 1314.00 | NIST | |
I | 1317.00 | NIST | |
I | 1316.00 | NIST | |
I | 1324.00 | NIST | |
I | 1298.00 | NIST | |
I | Outlier 1282.00 | NIST | |
I | 1328.00 | NIST | |
I | 1325.00 | NIST | |
I | 1322.00 | NIST | |
I | 1329.00 | NIST | |
I | 1318.00 | NIST | |
I | 1312.00 | NIST | |
I | 1330.00 | NIST | |
I | 1317.00 | NIST | |
I | 1316.00 | NIST | |
I | 1299.00 | NIST | |
I | 1316.00 | NIST | |
I | 1301.00 | NIST | |
I | 1298.00 | NIST | |
I | Outlier 1284.00 | NIST | |
I | 1297.00 | NIST | |
I | 1333.00 | NIST | |
I | 1318.00 | NIST | |
I | 1325.00 | NIST | |
I | 1330.00 | NIST | |
I | 1301.00 | NIST | |
I | Outlier 1347.00 | NIST | |
I | 1338.00 | NIST | |
Tboil | [420.65; 435.70] | K | |
Tboil | Outlier 435.70 | K | NIST |
Tboil | 424.80 | K | NIST |
Tboil | 425.00 | K | NIST |
Tboil | 425.35 ± 0.50 | K | NIST |
Tboil | 424.75 ± 1.00 | K | NIST |
Tboil | 424.15 ± 2.00 | K | NIST |
Tboil | 424.78 ± 0.20 | K | NIST |
Tboil | 425.15 ± 2.00 | K | NIST |
Tboil | 420.65 ± 3.00 | K | NIST |
Tboil | 420.65 ± 2.00 | K | NIST |
Tboil | 421.65 ± 3.00 | K | NIST |
Tboil | 421.15 ± 2.00 | K | NIST |
Tboil | 425.45 ± 0.50 | K | NIST |
Tboil | 426.15 ± 2.00 | K | NIST |
Tboil | 420.65 ± 3.00 | K | NIST |
Tboil | 421.00 ± 4.00 | K | NIST |
Tc | [603.50; 603.50] | K | |
Tc | 603.50 ± 0.70 | K | NIST |
Tc | 603.50 | K | NIST |
Tc | 603.50 | K | NIST |
Tfus | 203.20 | K | Joback Calculated Property |
Vc | 0.385 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [207.74; 261.25] | J/mol×K | [428.42; 592.97] | |
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 260 450 500 550 | ||||
Cp,gas | 207.74 | J/mol×K | 428.42 | Joback Calculated Property |
Cp,gas | 217.54 | J/mol×K | 455.85 | Joback Calculated Property |
Cp,gas | 226.97 | J/mol×K | 483.27 | Joback Calculated Property |
Cp,gas | 236.05 | J/mol×K | 510.70 | Joback Calculated Property |
Cp,gas | 244.78 | J/mol×K | 538.12 | Joback Calculated Property |
Cp,gas | 253.18 | J/mol×K | 565.55 | Joback Calculated Property |
Cp,gas | 261.25 | J/mol×K | 592.97 | Joback Calculated Property |
η | [0.0002400; 0.2179366] | Pa×s | [203.20; 428.42] | |
T(K) Dynamic viscosity (Pa×s) 0 0.05 0.1 0.15 0.2 200 300 400 | ||||
η | 0.2179366 | Pa×s | 203.20 | Joback Calculated Property |
η | 0.0289027 | Pa×s | 240.74 | Joback Calculated Property |
η | 0.0066108 | Pa×s | 278.27 | Joback Calculated Property |
η | 0.0021472 | Pa×s | 315.81 | Joback Calculated Property |
η | 0.0008856 | Pa×s | 353.35 | Joback Calculated Property |
η | 0.0004330 | Pa×s | 390.88 | Joback Calculated Property |
η | 0.0002400 | Pa×s | 428.42 | Joback Calculated Property |
ΔvapH | [44.46; 63.90] | kJ/mol | [360.50; 425.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 45 50 55 60 65 360 380 400 420 | ||||
ΔvapH | 46.50 | kJ/mol | 360.50 | NIST |
ΔvapH | 63.90 | kJ/mol | 362.50 | NIST |
ΔvapH | 53.00 | kJ/mol | 392.00 | NIST |
ΔvapH | 51.10 | kJ/mol | 399.00 | NIST |
ΔvapH | 44.46 | kJ/mol | 425.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [330.33; 445.83] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.46295e+01 | |||
Coefficient B | -3.07245e+03 | |||
Coefficient C | -1.16098e+02 | |||
Temperature range, min. | 330.33 | |||
Temperature range, max. | 445.83 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
Pvap | 1.33 | kPa | 330.33 | Calculated Property |
Pvap | 3.00 | kPa | 343.16 | Calculated Property |
Pvap | 6.19 | kPa | 356.00 | Calculated Property |
Pvap | 11.85 | kPa | 368.83 | Calculated Property |
Pvap | 21.33 | kPa | 381.66 | Calculated Property |
Pvap | 36.36 | kPa | 394.50 | Calculated Property |
Pvap | 59.13 | kPa | 407.33 | Calculated Property |
Pvap | 92.29 | kPa | 420.16 | Calculated Property |
Pvap | 138.95 | kPa | 433.00 | Calculated Property |
Pvap | 202.65 | kPa | 445.83 | Calculated Property |
Find more compounds similar to 1-Pentanol, 4-methyl-.
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