Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3340 | KDB | |
ΔcH°liquid | [-2000.70; -1997.60] | kJ/mol | |
ΔcH°liquid | -2000.70 ± 3.60 | kJ/mol | NIST |
ΔcH°liquid | -1997.60 ± 0.71 | kJ/mol | NIST |
ΔfG° | 7.49 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -121.29 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | [-183.20; -180.30] | kJ/mol | |
ΔfH°liquid | -180.30 ± 0.84 | kJ/mol | NIST |
ΔfH°liquid | -183.20 ± 0.71 | kJ/mol | NIST |
ΔfusH° | 11.36 | kJ/mol | Joback Calculated Property |
ΔvapH° | [41.30; 43.90] | kJ/mol | |
ΔvapH° | 43.90 | kJ/mol | NIST |
ΔvapH° | 41.30 ± 0.42 | kJ/mol | NIST |
IE | [10.48; 10.77] | eV | |
IE | 10.74 ± 0.03 | eV | NIST |
IE | 10.48 | eV | NIST |
IE | 10.77 ± 0.01 | eV | NIST |
IE | 10.71 ± 0.05 | eV | NIST |
log10WS | [-0.62; -0.62] | ||
log10WS | -0.62 | Aq. Sol... | |
log10WS | -0.62 | Estimat... | |
logPoct/wat | 0.671 | Crippen Calculated Property | |
McVol | 70.550 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
NFPA Health | 1 | KDB | |
NFPA Safety | 3 | KDB | |
Pc | 4150.00 | kPa | KDB |
Inp | [631.00; 686.00] | ||
Inp | Outlier 631.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 686.00 | NIST | |
Inp | 686.00 | NIST | |
Inp | 683.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 685.00 | NIST | |
Inp | 660.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 685.00 | NIST | |
I | [1109.00; 1129.00] | ||
I | 1129.00 | NIST | |
I | 1109.00 | NIST | |
I | 1109.00 | NIST | |
Tboil | [393.30; 393.50] | K | |
Tboil | 393.30 | K | KDB |
Tboil | 393.50 | K | NIST |
Tboil | 393.40 ± 0.05 | K | NIST |
Tboil | 393.50 ± 0.60 | K | NIST |
Tc | 597.00 | K | KDB |
Tfus | [180.00; 181.83] | K | |
Tfus | 180.72 | K | Aq. Sol... |
Tfus | 180.00 | K | KDB |
Tfus | 181.83 ± 0.05 | K | NIST |
Vc | 0.280 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [133.62; 176.19] | J/mol×K | [419.44; 634.16] | |
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 450 500 550 600 | ||||
Cp,gas | 133.62 | J/mol×K | 419.44 | Joback Calculated Property |
Cp,gas | 141.71 | J/mol×K | 455.23 | Joback Calculated Property |
Cp,gas | 149.38 | J/mol×K | 491.01 | Joback Calculated Property |
Cp,gas | 156.65 | J/mol×K | 526.80 | Joback Calculated Property |
Cp,gas | 163.54 | J/mol×K | 562.59 | Joback Calculated Property |
Cp,gas | 170.04 | J/mol×K | 598.37 | Joback Calculated Property |
Cp,gas | 176.19 | J/mol×K | 634.16 | Joback Calculated Property |
ΔvapH | [35.15; 40.90] | kJ/mol | [339.00; 393.30] | |
ΔvapH | 40.90 | kJ/mol | 339.00 | NIST |
ΔvapH | 35.15 | kJ/mol | 393.30 | KDB |
Pvap | [0.60; 5.61] | kPa | [274.70; 314.10] | |
T(K) Vapor pressure (kPa) 1 2 3 4 5 6 280 290 300 310 | ||||
Pvap | 0.61 | kPa | 274.70 | Aliphat... |
Pvap | 0.60 | kPa | 274.80 | Aliphat... |
Pvap | 0.60 | kPa | 274.80 | Aliphat... |
Pvap | 0.80 | kPa | 279.50 | Aliphat... |
Pvap | 0.83 | kPa | 279.60 | Aliphat... |
Pvap | 1.09 | kPa | 284.40 | Aliphat... |
Pvap | 1.09 | kPa | 284.40 | Aliphat... |
Pvap | 1.46 | kPa | 289.30 | Aliphat... |
Pvap | 1.95 | kPa | 294.20 | Aliphat... |
Pvap | 1.90 | kPa | 294.30 | Aliphat... |
Pvap | 2.57 | kPa | 299.20 | Aliphat... |
Pvap | 3.34 | kPa | 304.10 | Aliphat... |
Pvap | 3.34 | kPa | 304.20 | Aliphat... |
Pvap | 4.30 | kPa | 309.10 | Aliphat... |
Pvap | 5.61 | kPa | 314.10 | Aliphat... |
Pvap | 5.56 | kPa | 314.10 | Aliphat... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [288.38; 418.85] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.52250e+01 | |||
Coefficient B | -3.84564e+03 | |||
Coefficient C | -3.09300e+01 | |||
Temperature range, min. | 288.38 | |||
Temperature range, max. | 418.85 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 288.38 | Calculated Property |
Pvap | 2.96 | kPa | 302.88 | Calculated Property |
Pvap | 6.05 | kPa | 317.37 | Calculated Property |
Pvap | 11.54 | kPa | 331.87 | Calculated Property |
Pvap | 20.77 | kPa | 346.37 | Calculated Property |
Pvap | 35.49 | kPa | 360.86 | Calculated Property |
Pvap | 57.96 | kPa | 375.36 | Calculated Property |
Pvap | 90.98 | kPa | 389.86 | Calculated Property |
Pvap | 137.91 | kPa | 404.35 | Calculated Property |
Pvap | 202.65 | kPa | 418.85 | Calculated Property |
Pvap | [3.42e-05; 4339.63] | kPa | [181.83; 594.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.10809e+01 | |||
Coefficient B | -6.61815e+03 | |||
Coefficient C | -6.74802e+00 | |||
Coefficient D | 4.35069e-06 | |||
Temperature range, min. | 181.83 | |||
Temperature range, max. | 594.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 400 600 | ||||
Pvap | 3.42e-05 | kPa | 181.83 | Calculated Property |
Pvap | 0.01 | kPa | 227.63 | Calculated Property |
Pvap | 0.52 | kPa | 273.42 | Calculated Property |
Pvap | 6.58 | kPa | 319.22 | Calculated Property |
Pvap | 41.12 | kPa | 365.02 | Calculated Property |
Pvap | 163.17 | kPa | 410.81 | Calculated Property |
Pvap | 478.28 | kPa | 456.61 | Calculated Property |
Pvap | 1138.53 | kPa | 502.41 | Calculated Property |
Pvap | 2341.64 | kPa | 548.20 | Calculated Property |
Pvap | 4339.63 | kPa | 594.00 | Calculated Property |
Find more compounds similar to Propane, 2-nitro-.
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.