Property | Value | Unit | Source |
---|---|---|---|
PAff | 870.70 | kJ/mol | NIST |
BasG | 841.50 | kJ/mol | NIST |
ΔcH°liquid | -4648.30 ± 2.80 | kJ/mol | NIST |
ΔfG° | -96.54 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -358.00 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | -393.00 ± 3.00 | kJ/mol | NIST |
ΔfusH° | 4.14 | kJ/mol | Joback Calculated Property |
ΔvapH° | [34.40; 36.20] | kJ/mol | |
ΔvapH° | 34.67 | kJ/mol | NIST |
ΔvapH° | 36.20 | kJ/mol | NIST |
ΔvapH° | 34.40 ± 0.60 | kJ/mol | NIST |
ΔvapH° | 34.50 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 35.10 | kJ/mol | NIST |
IE | 9.20 | eV | NIST |
log10WS | -2.06 | Crippen Calculated Property | |
logPoct/wat | 2.210 | Crippen Calculated Property | |
McVol | 115.360 | ml/mol | McGowan Calculated Property |
Pc | 2829.33 | kPa | Joback Calculated Property |
Inp | [631.00; 668.00] | ||
Inp | 644.60 | NIST | |
Inp | 643.50 | NIST | |
Inp | 665.00 | NIST | |
Inp | 631.00 | NIST | |
Inp | 636.00 | NIST | |
Inp | 668.00 | NIST | |
Inp | 665.00 | NIST | |
Inp | 644.60 | NIST | |
I | [720.00; 724.00] | ||
I | 720.00 | NIST | |
I | 724.00 | NIST | |
I | 724.00 | NIST | |
Tboil | [360.70; 360.80] | K | |
Tboil | 360.80 | K | NIST |
Tboil | 360.70 | K | NIST |
Tboil | 360.80 ± 0.50 | K | NIST |
Tboil | 360.80 ± 0.40 | K | NIST |
Tc | 557.69 | K | Joback Calculated Property |
Tfus | 185.08 ± 0.20 | K | NIST |
Vc | 0.428 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [219.39; 291.56] | J/mol×K | [378.31; 557.69] | |
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 270 280 290 400 450 500 550 | ||||
Cp,gas | 219.39 | J/mol×K | 378.31 | Joback Calculated Property |
Cp,gas | 232.76 | J/mol×K | 408.21 | Joback Calculated Property |
Cp,gas | 245.58 | J/mol×K | 438.10 | Joback Calculated Property |
Cp,gas | 257.86 | J/mol×K | 468.00 | Joback Calculated Property |
Cp,gas | 269.60 | J/mol×K | 497.90 | Joback Calculated Property |
Cp,gas | 280.83 | J/mol×K | 527.80 | Joback Calculated Property |
Cp,gas | 291.56 | J/mol×K | 557.69 | Joback Calculated Property |
η | [0.0002455; 0.0142654] | Pa×s | [178.30; 378.31] | |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 0.01 200 250 300 350 | ||||
η | 0.0142654 | Pa×s | 178.30 | Joback Calculated Property |
η | 0.0042527 | Pa×s | 211.64 | Joback Calculated Property |
η | 0.0017624 | Pa×s | 244.97 | Joback Calculated Property |
η | 0.0009019 | Pa×s | 278.31 | Joback Calculated Property |
η | 0.0005327 | Pa×s | 311.64 | Joback Calculated Property |
η | 0.0003483 | Pa×s | 344.98 | Joback Calculated Property |
η | 0.0002455 | Pa×s | 378.31 | Joback Calculated Property |
ΔfusH | 8.46 | kJ/mol | 184.80 | NIST |
ΔvapH | [30.50; 34.00] | kJ/mol | [333.50; 360.70] | |
ΔvapH | 34.00 | kJ/mol | 333.50 | NIST |
ΔvapH | 30.50 | kJ/mol | 360.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [13.89; 103.54] | kPa | [306.15; 361.15] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.97222e+01 | |||
Coefficient B | -7.49443e+03 | |||
Coefficient C | -1.28665e+01 | |||
Coefficient D | 1.10706e-05 | |||
Temperature range, min. | 306.15 | |||
Temperature range, max. | 361.15 | |||
T(K) Vapor pressure (kPa) 20 40 60 80 100 320 340 360 | ||||
Pvap | 13.89 | kPa | 306.15 | Calculated Property |
Pvap | 18.14 | kPa | 312.26 | Calculated Property |
Pvap | 23.38 | kPa | 318.37 | Calculated Property |
Pvap | 29.79 | kPa | 324.48 | Calculated Property |
Pvap | 37.54 | kPa | 330.59 | Calculated Property |
Pvap | 46.82 | kPa | 336.71 | Calculated Property |
Pvap | 57.84 | kPa | 342.82 | Calculated Property |
Pvap | 70.81 | kPa | 348.93 | Calculated Property |
Pvap | 85.96 | kPa | 355.04 | Calculated Property |
Pvap | 103.54 | kPa | 361.15 | Calculated Property |
Find more compounds similar to Propane, 2-methyl-2-(1-methylethoxy)-.
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