Property | Value | Unit | Source |
---|---|---|---|
ω | 0.6040 | KDB | |
ΔcH°liquid | [-9824.10; -9822.10] | kJ/mol | |
ΔcH°liquid | -9824.10 ± 2.70 | kJ/mol | NIST |
ΔcH°liquid | -9822.10 ± 1.90 | kJ/mol | NIST |
ΔcH°solid | -9825.70 | kJ/mol | NIST |
ΔfG° | 111.90 | kJ/mol | KDB |
ΔfH°gas | -292.20 | kJ/mol | KDB |
ΔfH°liquid | -368.20 ± 2.10 | kJ/mol | NIST |
ΔfusH° | 28.54 | kJ/mol | Joback Calculated Property |
ΔvapH° | 75.70 | kJ/mol | NIST |
log10WS | -5.75 | Crippen Calculated Property | |
logPoct/wat | 5.707 | Crippen Calculated Property | |
McVol | 211.350 | ml/mol | McGowan Calculated Property |
Pc | 1630.00 | kPa | KDB |
Inp | [1536.30; 1550.00] | ||
Inp | 1536.30 | NIST | |
Inp | 1550.00 | NIST | |
S°gas | 688.06 | J/mol×K | NIST |
S°liquid | 538.52 | J/mol×K | NIST |
Tboil | [551.40; 552.50] | K | |
Tboil | 552.50 | K | KDB |
Tboil | 552.20 | K | NIST |
Tboil | 552.30 ± 0.30 | K | NIST |
Tboil | 551.40 ± 0.40 | K | NIST |
Tc | 730.60 | K | KDB |
Tfus | 251.10 | K | KDB |
Ttriple | 251.02 ± 0.01 | K | NIST |
Vc | 0.817 | m3/kmol | KDB |
Zc | 0.2190920 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [549.05; 662.54] | J/mol×K | [557.88; 737.70] | |
Cp,gas | 549.05 | J/mol×K | 557.88 | Joback Calculated Property |
Cp,gas | 570.35 | J/mol×K | 587.85 | Joback Calculated Property |
Cp,gas | 590.65 | J/mol×K | 617.82 | Joback Calculated Property |
Cp,gas | 609.98 | J/mol×K | 647.79 | Joback Calculated Property |
Cp,gas | 628.39 | J/mol×K | 677.76 | Joback Calculated Property |
Cp,gas | 645.89 | J/mol×K | 707.73 | Joback Calculated Property |
Cp,gas | 662.54 | J/mol×K | 737.70 | Joback Calculated Property |
Cp,liquid | 426.52 | J/mol×K | 298.15 | NIST |
η | [0.0002304; 0.0052655] | Pa×s | [269.71; 557.88] | |
η | 0.0052655 | Pa×s | 269.71 | Joback Calculated Property |
η | 0.0021076 | Pa×s | 317.74 | Joback Calculated Property |
η | 0.0010729 | Pa×s | 365.77 | Joback Calculated Property |
η | 0.0006389 | Pa×s | 413.79 | Joback Calculated Property |
η | 0.0004237 | Pa×s | 461.82 | Joback Calculated Property |
η | 0.0003037 | Pa×s | 509.85 | Joback Calculated Property |
η | 0.0002304 | Pa×s | 557.88 | Joback Calculated Property |
ΔfusH | [33.12; 33.14] | kJ/mol | [251.00; 251.02] | |
ΔfusH | 33.14 | kJ/mol | 251.00 | NIST |
ΔfusH | 33.14 | kJ/mol | 251.00 | NIST |
ΔfusH | 33.12 | kJ/mol | 251.02 | NIST |
ΔvapH | [48.99; 71.10] | kJ/mol | [384.50; 552.50] | |
ΔvapH | 71.10 | kJ/mol | 384.50 | NIST |
ΔvapH | 59.70 | kJ/mol | 503.00 | NIST |
ΔvapH | 48.99 | kJ/mol | 552.50 | KDB |
ρl | 811.00 | kg/m3 | 293.00 | KDB |
ΔfusS | 132.00 | J/mol×K | 251.02 | NIST |
γ | 0.03 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.29; 1633.09] | kPa | [413.00; 730.64] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.46330e+02 | |||
Coefficient B | -1.44632e+04 | |||
Coefficient C | -1.86364e+01 | |||
Coefficient D | 7.02517e-06 | |||
Temperature range, min. | 413.00 | |||
Temperature range, max. | 730.64 | |||
Pvap | 1.29 | kPa | 413.00 | Calculated Property |
Pvap | 5.45 | kPa | 448.29 | Calculated Property |
Pvap | 17.62 | kPa | 483.59 | Calculated Property |
Pvap | 46.48 | kPa | 518.88 | Calculated Property |
Pvap | 104.99 | kPa | 554.17 | Calculated Property |
Pvap | 210.49 | kPa | 589.47 | Calculated Property |
Pvap | 384.86 | kPa | 624.76 | Calculated Property |
Pvap | 655.33 | kPa | 660.05 | Calculated Property |
Pvap | 1056.40 | kPa | 695.35 | Calculated Property |
Pvap | 1633.09 | kPa | 730.64 | Calculated Property |
Find more compounds similar to Cyclopentane, decyl-.
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.