| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4034 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | [-1954.90; -1951.00] | kJ/mol |
|
| ΔcH°liquid | -1951.00 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -1954.90 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | -192.79 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | [-230.00; -226.00] | kJ/mol |
|
| ΔfH°liquid | -230.00 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -226.00 ± 2.00 | kJ/mol | NIST |
| ΔfusH° | 12.55 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 38.79 | kJ/mol | NIST |
| IE | 10.82 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.04 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.603 | Crippen Calculated Property | |
| McVol | 76.420 | ml/mol | McGowan Calculated Property |
| Pc | 4426.72 | kPa | Joback Calculated Property |
| Inp | [663.80; 693.00] |
|
|
| Inp | 663.80 | NIST | |
| Inp | 684.30 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 663.80 | NIST | |
| S°liquid | 263.20 | J/mol×K | NIST |
| Tboil | 373.70 | K | NIST |
| Tc | 551.13 | K | Relay (1.0) Calculated Property |
| Tfus | 201.86 | K | Relay (1.0) Calculated Property |
| Ttriple | 190.81 ± 0.02 | K | NIST |
Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [191.10; 200.70] | J/mol×K | [298.15; 350.00] | |
| Cp,liquid | 191.10 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 200.70 | J/mol×K | 350.00 | NIST |
| ΔfusH | [10.01; 10.10] | kJ/mol | [190.81; 190.90] | |
| ΔfusH | 10.01 | kJ/mol | 190.81 | NIST |
| ΔfusH | 10.10 | kJ/mol | 190.90 | NIST |
| ΔfusH | 10.10 | kJ/mol | 190.90 | NIST |
| ΔvapH | 39.70 | kJ/mol | 308.00 | NIST |
| ΔfusS | 52.43 | J/mol×K | 190.81 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [111.38; 239.37] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.94700e+01 | |||
| Coefficient B | 3.30900e-01 | |||
| Coefficient C | -1.10000e-04 | |||
| Coefficient D | -1.10000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 111.38 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 132.28 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 151.59 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 169.28 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 185.30 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 199.64 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 212.25 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 223.10 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 232.15 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 239.37 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [275.93; 397.59] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.48459e+01 | |||
| Coefficient B | -3.36152e+03 | |||
| Coefficient C | -4.50270e+01 | |||
| Temperature range, min. | 275.93 | |||
| Temperature range, max. | 397.59 | |||
| Pvap | 1.33 | kPa | 275.93 | Calculated Property |
| Pvap | 2.98 | kPa | 289.45 | Calculated Property |
| Pvap | 6.13 | kPa | 302.97 | Calculated Property |
| Pvap | 11.74 | kPa | 316.48 | Calculated Property |
| Pvap | 21.12 | kPa | 330.00 | Calculated Property |
| Pvap | 36.02 | kPa | 343.52 | Calculated Property |
| Pvap | 58.68 | kPa | 357.04 | Calculated Property |
| Pvap | 91.79 | kPa | 370.55 | Calculated Property |
| Pvap | 138.55 | kPa | 384.07 | Calculated Property |
| Pvap | 202.63 | kPa | 397.59 | Calculated Property |
| Pvap | [0.98; 33.50] | kPa | [273.00; 343.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.27677e+01 | |||
| Coefficient B | -2.34534e+03 | |||
| Coefficient C | -8.96220e+01 | |||
| Reference | Gray and Pratt, 1957, 3 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 343.00 | |||
| Pvap | 0.98 | kPa | 273.00 | Calculated Property |
| Pvap | 1.65 | kPa | 280.78 | Calculated Property |
| Pvap | 2.66 | kPa | 288.56 | Calculated Property |
| Pvap | 4.14 | kPa | 296.33 | Calculated Property |
| Pvap | 6.25 | kPa | 304.11 | Calculated Property |
| Pvap | 9.17 | kPa | 311.89 | Calculated Property |
| Pvap | 13.10 | kPa | 319.67 | Calculated Property |
| Pvap | 18.28 | kPa | 327.44 | Calculated Property |
| Pvap | 24.99 | kPa | 335.22 | Calculated Property |
| Pvap | 33.50 | kPa | 343.00 | Calculated Property |
| Pvap | [0.98; 33.50] | kPa | [273.00; 343.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.27677e+01 | |||
| Coefficient B | -2.34534e+03 | |||
| Coefficient C | -8.96220e+01 | |||
| Reference | Gray and Pratt, 1957 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 343.00 | |||
| Pvap | 0.98 | kPa | 273.00 | Calculated Property |
| Pvap | 1.65 | kPa | 280.78 | Calculated Property |
| Pvap | 2.66 | kPa | 288.56 | Calculated Property |
| Pvap | 4.14 | kPa | 296.33 | Calculated Property |
| Pvap | 6.25 | kPa | 304.11 | Calculated Property |
| Pvap | 9.17 | kPa | 311.89 | Calculated Property |
| Pvap | 13.10 | kPa | 319.67 | Calculated Property |
| Pvap | 18.28 | kPa | 327.44 | Calculated Property |
| Pvap | 24.99 | kPa | 335.22 | Calculated Property |
| Pvap | 33.50 | kPa | 343.00 | Calculated Property |
Find more compounds similar to Nitric acid, 1-methylethyl ester.
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