Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -61.09 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-42.00; -39.00] | kJ/mol |
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ΔfH°gas | -42.00 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | -39.00 | kJ/mol | NIST |
ΔfusH° | 8.81 | kJ/mol | Joback Calculated Property |
ΔvapH° | 36.11 | kJ/mol | Joback Calculated Property |
IE | [10.60; 11.05] | eV |
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IE | 11.05 ± 0.02 | eV | NIST |
IE | 10.60 | eV | NIST |
IE | 10.91 | eV | NIST |
log10WS | -2.73 | Crippen Calculated Property | |
logPoct/wat | 2.709 | Crippen Calculated Property | |
McVol | 79.170 | ml/mol | McGowan Calculated Property |
Pc | 5594.19 | kPa | Joback Calculated Property |
Inp | [750.00; 772.00] |
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|
Inp | 762.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 754.00 | NIST | |
Inp | 750.00 | NIST | |
Inp | 757.00 | NIST | |
I | [1070.00; 1101.23] |
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|
I | 1087.48 | NIST | |
I | 1101.23 | NIST | |
I | 1075.59 | NIST | |
I | 1070.00 | NIST | |
I | 1070.00 | NIST | |
Tboil | 376.65 ± 2.00 | K | NIST |
Tc | 629.91 | K | Joback Calculated Property |
Tfus | 268.00 ± 0.02 | K | NIST |
Vc | 0.289 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [92.41; 103.25] | J/mol×K | [397.50; 629.91] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 92 94 96 98 100 102 104 400 500 600 | ||||
Cp,gas | 92.41 | J/mol×K | 397.50 | Joback Calculated Property |
Cp,gas | 95.26 | J/mol×K | 436.23 | Joback Calculated Property |
Cp,gas | 97.63 | J/mol×K | 474.97 | Joback Calculated Property |
Cp,gas | 99.57 | J/mol×K | 513.70 | Joback Calculated Property |
Cp,gas | 101.12 | J/mol×K | 552.44 | Joback Calculated Property |
Cp,gas | 102.34 | J/mol×K | 591.17 | Joback Calculated Property |
Cp,gas | 103.25 | J/mol×K | 629.91 | Joback Calculated Property |
Cp,liquid | 149.40 | J/mol×K | 298.00 | NIST |
η | [0.0005797; 0.0046146] | Pa×s | [253.01; 397.50] | ![]() |
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 250 300 350 400 | ||||
η | 0.0046146 | Pa×s | 253.01 | Joback Calculated Property |
η | 0.0028102 | Pa×s | 277.09 | Joback Calculated Property |
η | 0.0018526 | Pa×s | 301.17 | Joback Calculated Property |
η | 0.0012990 | Pa×s | 325.25 | Joback Calculated Property |
η | 0.0009566 | Pa×s | 349.34 | Joback Calculated Property |
η | 0.0007328 | Pa×s | 373.42 | Joback Calculated Property |
η | 0.0005797 | Pa×s | 397.50 | Joback Calculated Property |
ΔfusH | [0.53; 4.62] | kJ/mol | [238.20; 267.90] | ![]() |
ΔfusH | 4.62 | kJ/mol | 238.20 | NIST |
ΔfusH | 0.53 | kJ/mol | 259.30 | NIST |
ΔfusH | 2.54 | kJ/mol | 267.50 | NIST |
ΔfusH | 2.03 | kJ/mol | 267.90 | NIST |
ΔvapH | [35.00; 36.10] | kJ/mol | [330.00; 368.50] | ![]() |
ΔvapH | 35.00 | kJ/mol | 330.00 | NIST |
ΔvapH | 36.10 | kJ/mol | 368.50 | NIST |
ρl | 2002.14 | kg/m3 | 298.15 | Vapour ... |
ΔfusS | [2.03; 19.40] | J/mol×K | [238.20; 267.90] | ![]() |
ΔfusS | 19.40 | J/mol×K | 238.20 | NIST |
ΔfusS | 2.03 | J/mol×K | 259.30 | NIST |
ΔfusS | 7.58 | J/mol×K | 267.90 | NIST |
csound,fluid | [863.60; 917.10] | m/s | [293.15; 313.15] | ![]() |
T(K) Speed of sound in fluid (m/s) 860 870 880 890 900 910 920 295 300 305 310 | ||||
csound,fluid | 917.10 | m/s | 293.15 | Excess ... |
csound,fluid | 917.10 | m/s | 293.15 | Excess ... |
csound,fluid | 917.10 | m/s | 293.15 | Excess ... |
csound,fluid | 903.60 | m/s | 298.15 | Excess ... |
csound,fluid | 903.60 | m/s | 298.15 | Excess ... |
csound,fluid | 903.60 | m/s | 298.15 | Excess ... |
csound,fluid | 890.20 | m/s | 303.15 | Excess ... |
csound,fluid | 890.20 | m/s | 303.15 | Excess ... |
csound,fluid | 890.20 | m/s | 303.15 | Excess ... |
csound,fluid | 876.80 | m/s | 308.15 | Excess ... |
csound,fluid | 876.80 | m/s | 308.15 | Excess ... |
csound,fluid | 876.80 | m/s | 308.15 | Excess ... |
csound,fluid | 863.60 | m/s | 313.15 | Excess ... |
csound,fluid | 863.60 | m/s | 313.15 | Excess ... |
csound,fluid | 863.60 | m/s | 313.15 | Excess ... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.35; 212.35] | kPa | [252.15; 404.31] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45069e+01 | |||
Coefficient B | -3.38195e+03 | |||
Coefficient C | -3.46430e+01 | |||
Temperature range, min. | 252.15 | |||
Temperature range, max. | 404.31 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 400 | ||||
Pvap | 0.35 | kPa | 252.15 | Calculated Property |
Pvap | 1.08 | kPa | 269.06 | Calculated Property |
Pvap | 2.86 | kPa | 285.96 | Calculated Property |
Pvap | 6.67 | kPa | 302.87 | Calculated Property |
Pvap | 14.10 | kPa | 319.78 | Calculated Property |
Pvap | 27.38 | kPa | 336.68 | Calculated Property |
Pvap | 49.57 | kPa | 353.59 | Calculated Property |
Pvap | 84.54 | kPa | 370.50 | Calculated Property |
Pvap | 136.97 | kPa | 387.40 | Calculated Property |
Pvap | 212.35 | kPa | 404.31 | Calculated Property |
Pvap | [0.35; 4916.26] | kPa | [252.15; 606.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.19744e+01 | |||
Coefficient B | -5.77070e+03 | |||
Coefficient C | -5.48617e+00 | |||
Coefficient D | 3.26165e-06 | |||
Temperature range, min. | 252.15 | |||
Temperature range, max. | 606.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 600 | ||||
Pvap | 0.35 | kPa | 252.15 | Calculated Property |
Pvap | 3.74 | kPa | 291.47 | Calculated Property |
Pvap | 21.28 | kPa | 330.78 | Calculated Property |
Pvap | 80.23 | kPa | 370.10 | Calculated Property |
Pvap | 227.76 | kPa | 409.42 | Calculated Property |
Pvap | 528.60 | kPa | 448.73 | Calculated Property |
Pvap | 1059.52 | kPa | 488.05 | Calculated Property |
Pvap | 1905.00 | kPa | 527.37 | Calculated Property |
Pvap | 3156.60 | kPa | 566.68 | Calculated Property |
Pvap | 4916.26 | kPa | 606.00 | Calculated Property |
Find more compounds similar to Methane, bromotrichloro-.
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