Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 130.67 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 12.54 | kJ/mol | Joback Calculated Property |
ΔfusH° | 19.11 | kJ/mol | Joback Calculated Property |
ΔvapH° | 53.63 | kJ/mol | Joback Calculated Property |
IE | 8.31 | eV | NIST |
log10WS | -3.94 | Crippen Calculated Property | |
logPoct/wat | 3.042 | Crippen Calculated Property | |
McVol | 138.290 | ml/mol | McGowan Calculated Property |
Pc | 3280.28 | kPa | Joback Calculated Property |
Inp | [1598.40; 1604.00] |
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|
Inp | 1598.40 | NIST | |
Inp | 1604.00 | NIST | |
Tboil | [573.70; 575.20] | K |
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Tboil | 573.70 | K | NIST |
Tboil | 575.20 | K | NIST |
Tboil | 575.00 ± 1.00 | K | NIST |
Tc | 817.23 | K | Joback Calculated Property |
Tfus | [325.20; 329.00] | K |
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Tfus | 329.00 | K | NIST |
Tfus | 325.20 ± 1.00 | K | NIST |
Vc | 0.527 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [313.12; 380.56] | J/mol×K | [578.47; 817.23] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 310 320 330 340 350 360 370 380 600 700 800 | ||||
Cp,gas | 313.12 | J/mol×K | 578.47 | Joback Calculated Property |
Cp,gas | 326.73 | J/mol×K | 618.26 | Joback Calculated Property |
Cp,gas | 339.29 | J/mol×K | 658.06 | Joback Calculated Property |
Cp,gas | 350.88 | J/mol×K | 697.85 | Joback Calculated Property |
Cp,gas | 361.57 | J/mol×K | 737.64 | Joback Calculated Property |
Cp,gas | 371.43 | J/mol×K | 777.44 | Joback Calculated Property |
Cp,gas | 380.56 | J/mol×K | 817.23 | Joback Calculated Property |
η | [0.0003556; 0.0017370] | Pa×s | [346.57; 578.47] | ![]() |
T(K) Dynamic viscosity (Pa×s) 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 1.80e-3 400 500 | ||||
η | 0.0017370 | Pa×s | 346.57 | Joback Calculated Property |
η | 0.0011679 | Pa×s | 385.22 | Joback Calculated Property |
η | 0.0008442 | Pa×s | 423.87 | Joback Calculated Property |
η | 0.0006442 | Pa×s | 462.52 | Joback Calculated Property |
η | 0.0005126 | Pa×s | 501.17 | Joback Calculated Property |
η | 0.0004214 | Pa×s | 539.82 | Joback Calculated Property |
η | 0.0003556 | Pa×s | 578.47 | Joback Calculated Property |
ΔsubH | [87.86; 87.90] | kJ/mol | [305.50; 328.80] | ![]() |
ΔsubH | 87.90 ± 0.40 | kJ/mol | 305.50 | NIST |
ΔsubH | 87.86 ± 0.42 | kJ/mol | 328.80 | NIST |
ΔvapH | 74.10 | kJ/mol | 483.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [445.00; 445.20] | K | [2.30; 2.30] |
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Tboilr | 445.20 | K | 2.30 | NIST |
Tboilr | 445.00 ± 1.00 | K | 2.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [446.52; 600.60] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.09370e+01 | |||
Coefficient B | -9.89570e+03 | |||
Coefficient C | 3.27040e+01 | |||
Temperature range, min. | 446.52 | |||
Temperature range, max. | 600.60 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 446.52 | Calculated Property |
Pvap | 2.72 | kPa | 463.64 | Calculated Property |
Pvap | 5.28 | kPa | 480.76 | Calculated Property |
Pvap | 9.84 | kPa | 497.88 | Calculated Property |
Pvap | 17.63 | kPa | 515.00 | Calculated Property |
Pvap | 30.48 | kPa | 532.12 | Calculated Property |
Pvap | 51.03 | kPa | 549.24 | Calculated Property |
Pvap | 82.96 | kPa | 566.36 | Calculated Property |
Pvap | 131.28 | kPa | 583.48 | Calculated Property |
Pvap | 202.65 | kPa | 600.60 | Calculated Property |
Find more compounds similar to 2-Naphthyl methyl ketone.
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