Property | Value | Unit | Source |
---|---|---|---|
IE | 8.55 | eV | NIST |
log10WS | -2.18 | Crippen Calculated Property | |
logPoct/wat | 2.365 | Crippen Calculated Property | |
McVol | 92.290 | ml/mol | McGowan Calculated Property |
Pc | 3908.00 | kPa | KDB |
Inp | [867.00; 908.10] |
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|
Inp | 890.00 | NIST | |
Inp | 887.00 | NIST | |
Inp | 883.50 | NIST | |
Inp | 885.00 | NIST | |
Inp | 898.00 | NIST | |
Inp | 888.00 | NIST | |
Inp | 887.00 | NIST | |
Inp | Outlier 908.10 | NIST | |
Inp | 889.00 | NIST | |
Inp | 882.00 | NIST | |
Inp | Outlier 867.00 | NIST | |
Inp | 888.00 | NIST | |
Inp | 882.00 | NIST | |
Inp | 883.00 | NIST | |
Inp | 882.00 | NIST | |
Inp | 883.00 | NIST | |
Inp | 889.00 | NIST | |
Inp | 888.00 | NIST | |
Inp | 881.00 | NIST | |
Inp | 881.00 | NIST | |
Inp | 885.00 | NIST | |
Inp | 890.00 | NIST | |
Inp | 888.00 | NIST | |
Inp | 889.00 | NIST | |
Inp | 883.00 | NIST | |
Inp | Outlier 908.10 | NIST | |
I | [1240.00; 1253.00] |
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|
I | 1250.00 | NIST | |
I | 1253.00 | NIST | |
I | 1253.00 | NIST | |
I | 1253.00 | NIST | |
I | 1240.00 | NIST | |
Tboil | [418.20; 418.20] | K |
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Tboil | 418.20 | K | KDB |
Tboil | 418.20 | K | NIST |
Tc | 640.20 | K | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ΔvapH | 41.10 | kJ/mol | 403.00 | NIST |
ρl | 1009.70 | kg/m3 | 293.10 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [307.42; 445.93] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42237e+01 | |||
Coefficient B | -3.42431e+03 | |||
Coefficient C | -6.17000e+01 | |||
Temperature range, min. | 307.42 | |||
Temperature range, max. | 445.93 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
Pvap | 1.33 | kPa | 307.42 | Calculated Property |
Pvap | 3.03 | kPa | 322.81 | Calculated Property |
Pvap | 6.29 | kPa | 338.20 | Calculated Property |
Pvap | 12.09 | kPa | 353.59 | Calculated Property |
Pvap | 21.75 | kPa | 368.98 | Calculated Property |
Pvap | 37.01 | kPa | 384.37 | Calculated Property |
Pvap | 60.00 | kPa | 399.76 | Calculated Property |
Pvap | 93.27 | kPa | 415.15 | Calculated Property |
Pvap | 139.73 | kPa | 430.54 | Calculated Property |
Pvap | 202.67 | kPa | 445.93 | Calculated Property |
Pvap | [4.40; 392.51] | kPa | [328.15; 478.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.23984e+01 | |||
Coefficient B | -7.87240e+03 | |||
Coefficient C | -9.93415e+00 | |||
Coefficient D | 5.82356e-06 | |||
Temperature range, min. | 328.15 | |||
Temperature range, max. | 478.15 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 400 350 400 450 | ||||
Pvap | 4.40 | kPa | 328.15 | Calculated Property |
Pvap | 9.16 | kPa | 344.82 | Calculated Property |
Pvap | 17.58 | kPa | 361.48 | Calculated Property |
Pvap | 31.53 | kPa | 378.15 | Calculated Property |
Pvap | 53.32 | kPa | 394.82 | Calculated Property |
Pvap | 85.75 | kPa | 411.48 | Calculated Property |
Pvap | 132.05 | kPa | 428.15 | Calculated Property |
Pvap | 195.88 | kPa | 444.82 | Calculated Property |
Pvap | 281.24 | kPa | 461.48 | Calculated Property |
Pvap | 392.51 | kPa | 478.15 | Calculated Property |
Find more compounds similar to Thiophene, 3,4-dimethyl-.
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