Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -3355.40 ± 4.20 | kJ/mol | NIST |
ΔfG° | -23.15 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -171.00 ± 8.80 | kJ/mol | NIST |
ΔfH°liquid | -208.00 ± 8.40 | kJ/mol | NIST |
ΔfusH° | 9.38 | kJ/mol | Joback Calculated Property |
ΔvapH° | [36.20; 38.10] | kJ/mol |
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ΔvapH° | 36.33 | kJ/mol | NIST |
ΔvapH° | 38.10 | kJ/mol | NIST |
ΔvapH° | 36.24 | kJ/mol | NIST |
ΔvapH° | 36.20 | kJ/mol | NIST |
ΔvapH° | 37.00 ± 1.00 | kJ/mol | NIST |
log10WS | -1.83 | Crippen Calculated Property | |
logPoct/wat | 2.271 | Crippen Calculated Property | |
McVol | 93.550 | ml/mol | McGowan Calculated Property |
Pc | 3352.86 | kPa | Joback Calculated Property |
Inp | [687.00; 723.00] |
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|
Inp | 696.00 | NIST | |
Inp | 688.00 | NIST | |
Inp | 691.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 697.00 | NIST | |
Inp | Outlier 723.00 | NIST | |
Inp | 687.00 | NIST | |
Inp | 690.00 | NIST | |
Inp | 706.00 | NIST | |
I | [880.00; 900.00] |
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|
I | 880.00 | NIST | |
I | 900.00 | NIST | |
I | 886.00 | NIST | |
I | 880.00 | NIST | |
Tboil | [371.25; 373.00] | K |
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Tboil | 372.00 | K | NIST |
Tboil | 372.55 ± 0.25 | K | NIST |
Tboil | Outlier 371.25 ± 1.00 | K | NIST |
Tboil | 372.50 ± 0.60 | K | NIST |
Tboil | 373.00 ± 0.50 | K | NIST |
Tboil | 372.40 ± 2.00 | K | NIST |
Tboil | 372.30 ± 0.15 | K | NIST |
Tc | 560.00 | K | NIST |
Tfus | 161.03 | K | Joback Calculated Property |
Vc | 0.358 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [150.99; 201.54] | J/mol×K | [350.79; 527.49] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 200 350 400 450 500 | ||||
Cp,gas | 150.99 | J/mol×K | 350.79 | Joback Calculated Property |
Cp,gas | 160.28 | J/mol×K | 380.24 | Joback Calculated Property |
Cp,gas | 169.22 | J/mol×K | 409.69 | Joback Calculated Property |
Cp,gas | 177.80 | J/mol×K | 439.14 | Joback Calculated Property |
Cp,gas | 186.05 | J/mol×K | 468.59 | Joback Calculated Property |
Cp,gas | 193.96 | J/mol×K | 498.04 | Joback Calculated Property |
Cp,gas | 201.54 | J/mol×K | 527.49 | Joback Calculated Property |
η | [0.0002823; 0.0078623] | Pa×s | [161.03; 350.79] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 8.00e-3 200 250 300 350 | ||||
η | 0.0078623 | Pa×s | 161.03 | Joback Calculated Property |
η | 0.0028647 | Pa×s | 192.66 | Joback Calculated Property |
η | 0.0013876 | Pa×s | 224.28 | Joback Calculated Property |
η | 0.0008040 | Pa×s | 255.91 | Joback Calculated Property |
η | 0.0005253 | Pa×s | 287.54 | Joback Calculated Property |
η | 0.0003734 | Pa×s | 319.16 | Joback Calculated Property |
η | 0.0002823 | Pa×s | 350.79 | Joback Calculated Property |
ΔvapH | [32.02; 35.40] | kJ/mol | [313.00; 372.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 32.5 33 33.5 34 34.5 35 35.5 320 340 360 | ||||
ΔvapH | 35.40 | kJ/mol | 313.00 | NIST |
ΔvapH | 34.60 | kJ/mol | 328.00 | NIST |
ΔvapH | 33.70 | kJ/mol | 343.00 | NIST |
ΔvapH | 32.80 | kJ/mol | 358.00 | NIST |
ΔvapH | 32.30 | kJ/mol | 368.00 | NIST |
ΔvapH | 32.02 | kJ/mol | 372.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [278.33; 394.44] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.54302e+01 | |||
Coefficient B | -3.54120e+03 | |||
Coefficient C | -4.44710e+01 | |||
Temperature range, min. | 278.33 | |||
Temperature range, max. | 394.44 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 278.33 | Calculated Property |
Pvap | 2.94 | kPa | 291.23 | Calculated Property |
Pvap | 6.00 | kPa | 304.13 | Calculated Property |
Pvap | 11.45 | kPa | 317.03 | Calculated Property |
Pvap | 20.60 | kPa | 329.93 | Calculated Property |
Pvap | 35.22 | kPa | 342.84 | Calculated Property |
Pvap | 57.59 | kPa | 355.74 | Calculated Property |
Pvap | 90.58 | kPa | 368.64 | Calculated Property |
Pvap | 137.59 | kPa | 381.54 | Calculated Property |
Pvap | 202.67 | kPa | 394.44 | Calculated Property |
Find more compounds similar to Butane, 1-chloro-3-methyl-.
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