Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -5096.90 ± 6.30 | kJ/mol | NIST |
ΔfG° | 300.87 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 234.00 ± 8.80 | kJ/mol | NIST |
ΔfH°liquid | 162.00 ± 6.30 | kJ/mol | NIST |
ΔfusH° | 16.73 | kJ/mol | Joback Calculated Property |
ΔvapH° | [69.90; 72.40] | kJ/mol |
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ΔvapH° | 69.90 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 72.40 ± 5.90 | kJ/mol | NIST |
IE | 8.03 | eV | NIST |
log10WS | [-4.55; -4.55] |
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log10WS | -4.55 | Aq. Sol... | |
log10WS | -4.55 | Estimat... | |
logPoct/wat | 3.444 | Crippen Calculated Property | |
McVol | 134.360 | ml/mol | McGowan Calculated Property |
Pc | 3722.56 | kPa | Joback Calculated Property |
Inp | [1571.90; 1571.90] |
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|
Inp | 1571.90 | NIST | |
Inp | 1571.90 | NIST | |
Tboil | 575.20 | K | NIST |
Tc | 846.27 | K | Joback Calculated Property |
Tfus | 280.00 ± 1.00 | K | NIST |
Vc | 0.497 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [254.13; 310.30] | J/mol×K | [571.98; 846.27] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 250 260 270 280 290 300 310 600 700 800 | ||||
Cp,gas | 254.13 | J/mol×K | 571.98 | Joback Calculated Property |
Cp,gas | 265.95 | J/mol×K | 617.70 | Joback Calculated Property |
Cp,gas | 276.61 | J/mol×K | 663.41 | Joback Calculated Property |
Cp,gas | 286.25 | J/mol×K | 709.13 | Joback Calculated Property |
Cp,gas | 294.99 | J/mol×K | 754.84 | Joback Calculated Property |
Cp,gas | 302.96 | J/mol×K | 800.56 | Joback Calculated Property |
Cp,gas | 310.30 | J/mol×K | 846.27 | Joback Calculated Property |
η | [0.0004067; 0.0020777] | Pa×s | [332.16; 571.98] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 400 500 | ||||
η | 0.0020777 | Pa×s | 332.16 | Joback Calculated Property |
η | 0.0013681 | Pa×s | 372.13 | Joback Calculated Property |
η | 0.0009769 | Pa×s | 412.10 | Joback Calculated Property |
η | 0.0007404 | Pa×s | 452.07 | Joback Calculated Property |
η | 0.0005870 | Pa×s | 492.04 | Joback Calculated Property |
η | 0.0004819 | Pa×s | 532.01 | Joback Calculated Property |
η | 0.0004067 | Pa×s | 571.98 | Joback Calculated Property |
ΔfusH | [15.91; 15.91] | kJ/mol | [280.00; 280.00] | ![]() |
ΔfusH | 15.91 | kJ/mol | 280.00 | NIST |
ΔfusH | 15.91 | kJ/mol | 280.00 | NIST |
ΔvapH | 78.90 | kJ/mol | 374.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 437.20 | K | 2.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [426.31; 637.74] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.28130e+01 | |||
Coefficient B | -3.95428e+03 | |||
Coefficient C | -1.10607e+02 | |||
Temperature range, min. | 426.31 | |||
Temperature range, max. | 637.74 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 426.31 | Calculated Property |
Pvap | 3.17 | kPa | 449.80 | Calculated Property |
Pvap | 6.76 | kPa | 473.29 | Calculated Property |
Pvap | 13.11 | kPa | 496.79 | Calculated Property |
Pvap | 23.59 | kPa | 520.28 | Calculated Property |
Pvap | 39.81 | kPa | 543.77 | Calculated Property |
Pvap | 63.68 | kPa | 567.26 | Calculated Property |
Pvap | 97.27 | kPa | 590.76 | Calculated Property |
Pvap | 142.82 | kPa | 614.25 | Calculated Property |
Pvap | 202.66 | kPa | 637.74 | Calculated Property |
Find more compounds similar to Naphthalene, 1-iodo-.
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