Property | Value | Unit | Source |
---|---|---|---|
ΔcH°gas | -3193.60 ± 0.88 | kJ/mol | NIST |
ΔfG° | 159.28 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 82.72 ± 0.92 | kJ/mol | NIST |
ΔfusH° | 7.63 | kJ/mol | Joback Calculated Property |
ΔvapH° | 28.30 | kJ/mol | NIST |
IE | [8.59; 8.67] | eV |
![]() |
IE | 8.62 ± 0.03 | eV | NIST |
IE | 8.64 | eV | NIST |
IE | 8.67 ± 0.02 | eV | NIST |
IE | 8.59 | eV | NIST |
IE | 8.63 | eV | NIST |
IE | 8.60 | eV | NIST |
IE | 8.60 | eV | NIST |
log10WS | -1.62 | Crippen Calculated Property | |
logPoct/wat | 1.748 | Crippen Calculated Property | |
McVol | 72.710 | ml/mol | McGowan Calculated Property |
Pc | 3886.79 | kPa | Joback Calculated Property |
Inp | [510.00; 541.20] |
![]() |
|
Inp | 524.00 | NIST | |
Inp | 537.00 | NIST | |
Inp | Outlier 510.00 | NIST | |
Inp | 525.00 | NIST | |
Inp | 524.80 | NIST | |
Inp | 524.40 | NIST | |
Inp | 525.10 | NIST | |
Inp | 536.10 | NIST | |
Inp | 522.80 | NIST | |
Inp | 524.00 | NIST | |
Inp | 525.00 | NIST | |
Inp | 527.00 | NIST | |
Inp | 527.00 | NIST | |
Inp | 541.20 | NIST | |
Inp | Outlier 510.50 | NIST | |
Inp | 536.00 | NIST | |
Inp | 524.00 | NIST | |
Inp | 536.00 | NIST | |
Inp | 536.00 | NIST | |
Inp | 532.00 | NIST | |
Inp | 536.00 | NIST | |
S°gas | 322.80 | J/mol×K | NIST |
S°liquid | 233.25 | J/mol×K | NIST |
Tboil | [316.00; 317.30] | K |
![]() |
Tboil | 317.30 | K | NIST |
Tboil | 317.18 ± 0.40 | K | NIST |
Tboil | 317.20 ± 0.40 | K | NIST |
Tboil | 316.65 ± 1.00 | K | NIST |
Tboil | 316.00 ± 2.00 | K | NIST |
Tc | 490.29 | K | Joback Calculated Property |
Tfus | [131.57; 132.33] | K |
![]() |
Tfus | 132.31 | K | KDB |
Tfus | 132.31 ± 0.04 | K | NIST |
Tfus | 132.31 ± 0.03 | K | NIST |
Tfus | 132.33 ± 0.02 | K | NIST |
Tfus | 131.57 ± 0.50 | K | NIST |
Ttriple | 132.35 ± 0.05 | K | NIST |
Vc | 0.277 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [100.21; 143.95] | J/mol×K | [314.64; 490.29] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 100 110 120 130 140 350 400 450 | ||||
Cp,gas | 100.21 | J/mol×K | 314.64 | Joback Calculated Property |
Cp,gas | 108.47 | J/mol×K | 343.91 | Joback Calculated Property |
Cp,gas | 116.31 | J/mol×K | 373.19 | Joback Calculated Property |
Cp,gas | 123.76 | J/mol×K | 402.46 | Joback Calculated Property |
Cp,gas | 130.84 | J/mol×K | 431.74 | Joback Calculated Property |
Cp,gas | 137.57 | J/mol×K | 461.01 | Joback Calculated Property |
Cp,gas | 143.95 | J/mol×K | 490.29 | Joback Calculated Property |
Cp,liquid | 146.57 | J/mol×K | 298.15 | NIST |
η | [0.0001562; 0.0024945] | Pa×s | [139.27; 314.64] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 150 200 250 300 | ||||
η | 0.0024945 | Pa×s | 139.27 | Joback Calculated Property |
η | 0.0010531 | Pa×s | 168.50 | Joback Calculated Property |
η | 0.0005737 | Pa×s | 197.73 | Joback Calculated Property |
η | 0.0003655 | Pa×s | 226.95 | Joback Calculated Property |
η | 0.0002581 | Pa×s | 256.18 | Joback Calculated Property |
η | 0.0001957 | Pa×s | 285.41 | Joback Calculated Property |
η | 0.0001562 | Pa×s | 314.64 | Joback Calculated Property |
ΔfusH | [5.64; 5.64] | kJ/mol | [132.35; 132.40] | ![]() |
ΔfusH | 5.64 | kJ/mol | 132.35 | NIST |
ΔfusH | 5.64 | kJ/mol | 132.40 | NIST |
ΔfusH | 5.64 | kJ/mol | 132.40 | NIST |
ΔvapH | [28.80; 31.90] | kJ/mol | [227.50; 303.50] | ![]() |
ΔvapH | 31.90 | kJ/mol | 227.50 | NIST |
ΔvapH | 31.20 | kJ/mol | 242.50 | NIST |
ΔvapH | 30.10 | kJ/mol | 290.50 | NIST |
ΔvapH | 28.80 | kJ/mol | 303.50 | NIST |
ΔfusS | 42.60 | J/mol×K | 132.35 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [227.24; 340.25] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.37915e+01 | |||
Coefficient B | -2.57592e+03 | |||
Coefficient C | -3.64890e+01 | |||
Temperature range, min. | 227.24 | |||
Temperature range, max. | 340.25 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 1.33 | kPa | 227.24 | Calculated Property |
Pvap | 3.07 | kPa | 239.80 | Calculated Property |
Pvap | 6.41 | kPa | 252.35 | Calculated Property |
Pvap | 12.36 | kPa | 264.91 | Calculated Property |
Pvap | 22.24 | kPa | 277.47 | Calculated Property |
Pvap | 37.77 | kPa | 290.02 | Calculated Property |
Pvap | 61.00 | kPa | 302.58 | Calculated Property |
Pvap | 94.36 | kPa | 315.14 | Calculated Property |
Pvap | 140.57 | kPa | 327.69 | Calculated Property |
Pvap | 202.63 | kPa | 340.25 | Calculated Property |
Pvap | [2.08e-06; 3762.04] | kPa | [132.35; 499.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.03742e+01 | |||
Coefficient B | -5.30049e+03 | |||
Coefficient C | -6.85336e+00 | |||
Coefficient D | 4.24873e-06 | |||
Temperature range, min. | 132.35 | |||
Temperature range, max. | 499.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 500 | ||||
Pvap | 2.08e-06 | kPa | 132.35 | Calculated Property |
Pvap | 4.33e-03 | kPa | 173.09 | Calculated Property |
Pvap | 0.37 | kPa | 213.83 | Calculated Property |
Pvap | 6.45 | kPa | 254.57 | Calculated Property |
Pvap | 45.31 | kPa | 295.31 | Calculated Property |
Pvap | 183.68 | kPa | 336.04 | Calculated Property |
Pvap | 522.06 | kPa | 376.78 | Calculated Property |
Pvap | 1169.45 | kPa | 417.52 | Calculated Property |
Pvap | 2222.53 | kPa | 458.26 | Calculated Property |
Pvap | 3762.04 | kPa | 499.00 | Calculated Property |
Find more compounds similar to 1,3-Pentadiene, (Z)-.
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.