Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -2206.50 ± 0.60 | kJ/mol | NIST |
ΔfG° | -307.92 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -532.40 ± 1.80 | kJ/mol | NIST |
ΔfH°solid | -618.50 ± 0.90 | kJ/mol | NIST |
ΔfusH° | 6.47 | kJ/mol | Joback Calculated Property |
ΔsubH° | [86.10; 86.10] | kJ/mol |
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ΔsubH° | 86.10 ± 1.60 | kJ/mol | NIST |
ΔsubH° | 86.10 ± 1.60 | kJ/mol | NIST |
ΔsubH° | 86.10 | kJ/mol | NIST |
ΔvapH° | 40.47 | kJ/mol | Joback Calculated Property |
IE | 11.17 | eV | NIST |
log10WS | -0.45 | Crippen Calculated Property | |
logPoct/wat | 0.240 | Crippen Calculated Property | |
McVol | 79.460 | ml/mol | McGowan Calculated Property |
Pc | 5109.34 | kPa | Joback Calculated Property |
Tboil | 560.15 | K | NIST |
Tc | 749.54 | K | Joback Calculated Property |
Tfus | 325.15 | K | NIST |
Ttriple | 329.20 | K | Solubil... |
Vc | 0.284 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [171.81; 236.02] | J/mol×K | [500.61; 749.54] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 220 230 240 500 600 700 | ||||
Cp,gas | 171.81 | J/mol×K | 500.61 | Joback Calculated Property |
Cp,gas | 183.79 | J/mol×K | 542.10 | Joback Calculated Property |
Cp,gas | 195.35 | J/mol×K | 583.59 | Joback Calculated Property |
Cp,gas | 206.42 | J/mol×K | 625.08 | Joback Calculated Property |
Cp,gas | 216.93 | J/mol×K | 666.56 | Joback Calculated Property |
Cp,gas | 226.82 | J/mol×K | 708.05 | Joback Calculated Property |
Cp,gas | 236.02 | J/mol×K | 749.54 | Joback Calculated Property |
ΔsubH | 85.90 ± 1.60 | kJ/mol | 309.00 | NIST |
ΔvapH | 60.90 | kJ/mol | 466.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [423.20; 440.50] | K | [1.30; 2.70] |
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Tboilr | 423.20 | K | 1.30 | NIST |
Tboilr | 440.50 ± 2.50 | K | 2.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [423.88; 597.14] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.60108e+01 | |||
Coefficient B | -5.80167e+03 | |||
Coefficient C | -5.48940e+01 | |||
Temperature range, min. | 423.88 | |||
Temperature range, max. | 597.14 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 423.88 | Calculated Property |
Pvap | 2.91 | kPa | 443.13 | Calculated Property |
Pvap | 5.89 | kPa | 462.38 | Calculated Property |
Pvap | 11.19 | kPa | 481.63 | Calculated Property |
Pvap | 20.13 | kPa | 500.88 | Calculated Property |
Pvap | 34.49 | kPa | 520.14 | Calculated Property |
Pvap | 56.60 | kPa | 539.39 | Calculated Property |
Pvap | 89.45 | kPa | 558.64 | Calculated Property |
Pvap | 136.68 | kPa | 577.89 | Calculated Property |
Pvap | 202.64 | kPa | 597.14 | Calculated Property |
Pvap | [5.12e-03; 5786.20] | kPa | [328.00; 838.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.65423e+01 | |||
Coefficient B | -1.19239e+04 | |||
Coefficient C | -1.13780e+01 | |||
Coefficient D | 4.18011e-06 | |||
Temperature range, min. | 328.00 | |||
Temperature range, max. | 838.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 400 600 800 | ||||
Pvap | 5.12e-03 | kPa | 328.00 | Calculated Property |
Pvap | 0.21 | kPa | 384.67 | Calculated Property |
Pvap | 2.85 | kPa | 441.33 | Calculated Property |
Pvap | 19.51 | kPa | 498.00 | Calculated Property |
Pvap | 84.82 | kPa | 554.67 | Calculated Property |
Pvap | 271.12 | kPa | 611.33 | Calculated Property |
Pvap | 700.37 | kPa | 668.00 | Calculated Property |
Pvap | 1557.57 | kPa | 724.67 | Calculated Property |
Pvap | 3116.07 | kPa | 781.33 | Calculated Property |
Pvap | 5786.20 | kPa | 838.00 | Calculated Property |
Find more compounds similar to 2H-Pyran-2,6(3H)-dione, dihydro-.
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