Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4510 | KDB | |
AP | 351.350 | K | KDB |
ΔfG° | 30.88 | kJ/mol | Joback Calculated Property |
Δc,grossH | 6775.15 | kJ/mol | KDB |
Δc,netH | 6291.021 | kJ/mol | KDB |
ΔfH°gas | -255.01 | kJ/mol | Joback Calculated Property |
ΔfusH° | 18.13 | kJ/mol | Joback Calculated Property |
ΔvapH° | [49.72; 50.20] | kJ/mol | |
ΔvapH° | 49.72 | kJ/mol | NIST |
ΔvapH° | 50.20 | kJ/mol | NIST |
log10WS | -3.77 | Crippen Calculated Property | |
logPoct/wat | 4.003 | Crippen Calculated Property | |
McVol | 151.760 | ml/mol | McGowan Calculated Property |
Pc | 2140.00 | kPa | KDB |
Inp | [958.00; 980.00] | ||
Inp | 970.40 | NIST | |
Inp | 970.50 | NIST | |
Inp | 970.00 | NIST | |
Inp | 967.00 | NIST | |
Inp | 967.00 | NIST | |
Inp | 967.00 | NIST | |
Inp | Outlier 979.00 | NIST | |
Inp | 974.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | Outlier 980.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | 971.20 | NIST | |
Inp | 971.30 | NIST | |
Inp | 973.00 | NIST | |
Inp | 970.40 | NIST | |
Inp | 970.40 | NIST | |
Inp | 970.60 | NIST | |
Inp | 972.50 | NIST | |
Inp | 970.40 | NIST | |
Inp | 971.30 | NIST | |
Inp | 969.60 | NIST | |
Inp | 970.20 | NIST | |
Inp | 973.00 | NIST | |
Inp | Outlier 958.00 | NIST | |
Inp | 970.42 | NIST | |
Inp | 970.42 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 977.00 | NIST | |
Inp | 971.92 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 977.20 | NIST | |
Inp | Outlier 979.00 | NIST | |
Inp | 969.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | Outlier 962.00 | NIST | |
Inp | 972.80 | NIST | |
Inp | 969.00 | NIST | |
Inp | 971.20 | NIST | |
Inp | 970.50 | NIST | |
Inp | 971.70 | NIST | |
Inp | 974.20 | NIST | |
Inp | 972.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 971.80 | NIST | |
Inp | 972.15 | NIST | |
Inp | 972.23 | NIST | |
Inp | 971.40 | NIST | |
Inp | 971.74 | NIST | |
Inp | 971.85 | NIST | |
Inp | 970.00 | NIST | |
Inp | 968.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | Outlier 960.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 969.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 975.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 974.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 972.10 | NIST | |
Inp | 967.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | Outlier 964.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | 966.00 | NIST | |
Inp | 968.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 966.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 971.40 | NIST | |
Inp | 977.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 966.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 969.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | 970.00 | NIST | |
I | [965.00; 983.00] | ||
I | 983.00 | NIST | |
I | 969.00 | NIST | |
I | 965.00 | NIST | |
I | 983.00 | NIST | |
I | 969.00 | NIST | |
S°liquid | 427.20 | J/mol×K | NIST |
Tboil | 441.00 | K | KDB |
Tc | [613.40; 613.60] | K | |
Tc | 613.40 | K | KDB |
Tc | 613.60 | K | NIST |
Tfus | [183.15; 188.49] | K | |
Tfus | 188.00 | K | KDB |
Tfus | 188.49 ± 0.20 | K | NIST |
Tfus | 183.15 ± 0.50 | K | NIST |
Tfus | 188.29 ± 0.20 | K | NIST |
Ttriple | 188.50 ± 0.20 | K | NIST |
Vc | 0.582 | m3/kmol | KDB |
Zc | 0.2442060 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [315.29; 399.91] | J/mol×K | [427.76; 593.73] | |
Cp,gas | 315.29 | J/mol×K | 427.76 | Joback Calculated Property |
Cp,gas | 330.79 | J/mol×K | 455.42 | Joback Calculated Property |
Cp,gas | 345.71 | J/mol×K | 483.08 | Joback Calculated Property |
Cp,gas | 360.07 | J/mol×K | 510.75 | Joback Calculated Property |
Cp,gas | 373.88 | J/mol×K | 538.41 | Joback Calculated Property |
Cp,gas | 387.16 | J/mol×K | 566.07 | Joback Calculated Property |
Cp,gas | 399.91 | J/mol×K | 593.73 | Joback Calculated Property |
Cp,liquid | 308.99 | J/mol×K | 298.10 | NIST |
η | [0.0002265; 0.0108083] | Pa×s | [187.46; 427.76] | |
η | 0.0108083 | Pa×s | 187.46 | Joback Calculated Property |
η | 0.0032190 | Pa×s | 227.51 | Joback Calculated Property |
η | 0.0013777 | Pa×s | 267.56 | Joback Calculated Property |
η | 0.0007355 | Pa×s | 307.61 | Joback Calculated Property |
η | 0.0004537 | Pa×s | 347.66 | Joback Calculated Property |
η | 0.0003093 | Pa×s | 387.71 | Joback Calculated Property |
η | 0.0002265 | Pa×s | 427.76 | Joback Calculated Property |
ΔfusH | [18.70; 18.70] | kJ/mol | [188.50; 188.50] | |
ΔfusH | 18.70 | kJ/mol | 188.50 | NIST |
ΔfusH | 18.70 | kJ/mol | 188.50 | NIST |
ΔvapH | [38.26; 47.30] | kJ/mol | [328.00; 441.00] | |
ΔvapH | 47.30 ± 0.20 | kJ/mol | 328.00 | NIST |
ΔvapH | 46.20 ± 0.20 | kJ/mol | 343.00 | NIST |
ΔvapH | 45.10 ± 0.20 | kJ/mol | 358.00 | NIST |
ΔvapH | 39.12 | kJ/mol | 441.00 | KDB |
ΔvapH | 38.26 | kJ/mol | 441.00 | NIST |
n0 | 1.41030 | 298.15 | KDB | |
ΔfusS | 99.20 | J/mol×K | 188.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [323.99; 469.90] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45072e+01 | |||
Coefficient B | -3.79773e+03 | |||
Coefficient C | -5.69090e+01 | |||
Temperature range, min. | 323.99 | |||
Temperature range, max. | 469.90 | |||
Pvap | 1.33 | kPa | 323.99 | Calculated Property |
Pvap | 3.01 | kPa | 340.20 | Calculated Property |
Pvap | 6.22 | kPa | 356.41 | Calculated Property |
Pvap | 11.92 | kPa | 372.63 | Calculated Property |
Pvap | 21.45 | kPa | 388.84 | Calculated Property |
Pvap | 36.55 | kPa | 405.05 | Calculated Property |
Pvap | 59.38 | kPa | 421.26 | Calculated Property |
Pvap | 92.58 | kPa | 437.48 | Calculated Property |
Pvap | 139.18 | kPa | 453.69 | Calculated Property |
Pvap | 202.66 | kPa | 469.90 | Calculated Property |
Pvap | [5.74e-07; 2188.73] | kPa | [188.35; 613.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.11505e+02 | |||
Coefficient B | -9.76977e+03 | |||
Coefficient C | -1.41847e+01 | |||
Coefficient D | 8.42650e-06 | |||
Temperature range, min. | 188.35 | |||
Temperature range, max. | 613.00 | |||
Pvap | 5.74e-07 | kPa | 188.35 | Calculated Property |
Pvap | 9.29e-04 | kPa | 235.53 | Calculated Property |
Pvap | 0.09 | kPa | 282.72 | Calculated Property |
Pvap | 1.74 | kPa | 329.90 | Calculated Property |
Pvap | 14.07 | kPa | 377.08 | Calculated Property |
Pvap | 64.82 | kPa | 424.27 | Calculated Property |
Pvap | 207.81 | kPa | 471.45 | Calculated Property |
Pvap | 524.56 | kPa | 518.63 | Calculated Property |
Pvap | 1129.44 | kPa | 565.82 | Calculated Property |
Pvap | 2188.73 | kPa | 613.00 | Calculated Property |
Find more compounds similar to Nonane, 3-methyl-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.