Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1990 | KDB | |
PAff | 628.00 ± 8.00 | kJ/mol | NIST |
BasG | 602.00 ± 8.00 | kJ/mol | NIST |
ΔcH°liquid | [-605.80; -602.50] | kJ/mol |
![]() |
ΔcH°liquid | -602.50 | kJ/mol | NIST |
ΔcH°liquid | -605.80 ± 8.40 | kJ/mol | NIST |
μ | 1.80 | debye | KDB |
ΔfG° | -68.91 | kJ/mol | KDB |
Rg | 2.4320 | KDB | |
ΔfH°gas | [-95.70; -95.10] | kJ/mol |
![]() |
ΔfH°gas | -95.46 | kJ/mol | KDB |
ΔfH°gas | -95.10 ± 2.50 | kJ/mol | NIST |
ΔfH°gas | -95.70 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | [-124.30; -124.10] | kJ/mol |
![]() |
ΔfH°liquid | -124.10 ± 2.50 | kJ/mol | NIST |
ΔfH°liquid | -124.30 | kJ/mol | NIST |
ΔfusH° | 6.74 | kJ/mol | Joback Calculated Property |
ΔvapH° | [28.50; 30.60] | kJ/mol |
![]() |
ΔvapH° | 29.00 | kJ/mol | NIST |
ΔvapH° | 29.03 ± 0.08 | kJ/mol | NIST |
ΔvapH° | 30.60 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 28.80 | kJ/mol | NIST |
ΔvapH° | 28.50 ± 0.42 | kJ/mol | NIST |
IE | [11.28; 11.40] | eV |
![]() |
IE | 11.33 ± 0.04 | eV | NIST |
IE | 11.32 | eV | NIST |
IE | 11.40 | eV | NIST |
IE | 11.32 ± 0.01 | eV | NIST |
IE | 11.28 | eV | NIST |
IE | 11.33 | eV | NIST |
IE | 11.36 | eV | NIST |
IE | 11.35 ± 0.02 | eV | NIST |
IE | 11.40 | eV | NIST |
log10WS | [-0.63; -0.63] |
![]() |
|
log10WS | -0.63 | Aq. Sol... | |
log10WS | -0.63 | Estimat... | |
logPoct/wat | 1.421 | Crippen Calculated Property | |
McVol | 49.430 | ml/mol | McGowan Calculated Property |
NFPA Health | 2 | KDB | |
Pc | [6100.00; 6355.00] | kPa |
![]() |
Pc | 6100.00 | kPa | KDB |
Pc | 6355.00 ± 15.00 | kPa | NIST |
Inp | [477.00; 555.90] |
![]() |
|
Inp | Outlier 553.50 | NIST | |
Inp | Outlier 555.90 | NIST | |
Inp | Outlier 553.70 | NIST | |
Inp | 548.40 | NIST | |
Inp | 542.20 | NIST | |
Inp | 506.30 | NIST | |
Inp | 518.00 | NIST | |
Inp | 504.90 | NIST | |
Inp | 508.00 | NIST | |
Inp | 516.90 | NIST | |
Inp | 516.50 | NIST | |
Inp | 537.80 | NIST | |
Inp | 537.90 | NIST | |
Inp | 519.00 | NIST | |
Inp | 520.00 | NIST | |
Inp | 518.00 | NIST | |
Inp | Outlier 486.00 | NIST | |
Inp | 524.00 | NIST | |
Inp | 497.90 | NIST | |
Inp | Outlier 477.00 | NIST | |
Inp | 511.00 | NIST | |
Inp | 513.00 | NIST | |
Inp | 531.00 | NIST | |
Inp | 540.00 | NIST | |
Inp | 540.00 | NIST | |
Inp | 510.00 | NIST | |
Inp | 512.70 | NIST | |
Inp | 531.60 | NIST | |
Inp | 524.00 | NIST | |
Inp | 520.00 | NIST | |
Inp | Outlier 480.00 | NIST | |
Inp | Outlier 488.00 | NIST | |
Inp | 531.00 | NIST | |
Inp | 531.00 | NIST | |
Inp | 528.00 | NIST | |
Inp | 514.00 | NIST | |
Inp | 520.00 | NIST | |
Inp | 511.00 | NIST | |
Inp | 527.00 | NIST | |
Inp | 528.00 | NIST | |
Inp | 529.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 519.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 531.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 512.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 504.00 | NIST | |
Inp | 510.00 | NIST | |
Inp | 527.00 | NIST | |
Inp | 530.00 | NIST | |
Inp | 524.00 | NIST | |
Inp | 524.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 531.00 | NIST | |
Inp | 511.00 | NIST | |
Inp | 512.70 | NIST | |
I | [905.00; 953.00] |
![]() |
|
I | 948.00 | NIST | |
I | 946.00 | NIST | |
I | 935.70 | NIST | |
I | 932.62 | NIST | |
I | 926.65 | NIST | |
I | 933.00 | NIST | |
I | 933.00 | NIST | |
I | 914.00 | NIST | |
I | 925.00 | NIST | |
I | 931.00 | NIST | |
I | 948.00 | NIST | |
I | 948.00 | NIST | |
I | Outlier 905.00 | NIST | |
I | 937.20 | NIST | |
I | 936.00 | NIST | |
I | 927.00 | NIST | |
I | 933.00 | NIST | |
I | 953.00 | NIST | |
I | 944.00 | NIST | |
I | 932.00 | NIST | |
I | 937.00 | NIST | |
I | 944.00 | NIST | |
I | 933.00 | NIST | |
I | 919.00 | NIST | |
I | 925.00 | NIST | |
I | 928.00 | NIST | |
I | 912.00 | NIST | |
I | 927.00 | NIST | |
I | 933.00 | NIST | |
I | 914.00 | NIST | |
I | 917.00 | NIST | |
I | 937.20 | NIST | |
I | 948.00 | NIST | |
I | 933.00 | NIST | |
S°liquid | 174.50 | J/mol×K | NIST |
Tboil | [312.92; 314.95] | K |
![]() |
Tboil | 313.00 | K | KDB |
Tboil | 312.93 ± 0.20 | K | NIST |
Tboil | 313.00 | K | NIST |
Tboil | 312.92 ± 0.07 | K | NIST |
Tboil | 313.30 ± 0.30 | K | NIST |
Tboil | 312.95 ± 0.50 | K | NIST |
Tboil | 313.15 ± 1.00 | K | NIST |
Tboil | 313.20 ± 0.50 | K | NIST |
Tboil | 313.20 ± 1.00 | K | NIST |
Tboil | 313.35 ± 0.20 | K | NIST |
Tboil | 312.95 ± 0.30 | K | NIST |
Tboil | Outlier 314.70 ± 0.50 | K | NIST |
Tboil | Outlier 314.95 ± 0.50 | K | NIST |
Tc | [508.00; 510.00] | K |
![]() |
Tc | 510.00 | K | KDB |
Tc | 508.00 ± 0.20 | K | NIST |
Tc | 510.00 | K | NIST |
Tfus | [176.00; 198.06] | K |
![]() |
Tfus | 178.01 | K | KDB |
Tfus | 177.62 | K | Aq. Sol... |
Tfus | Outlier 198.06 ± 0.40 | K | NIST |
Tfus | 176.00 ± 1.50 | K | NIST |
Tfus | 177.00 ± 2.00 | K | NIST |
Tfus | 176.65 ± 0.40 | K | NIST |
Vc | 0.190 | m3/kmol | Joback Calculated Property |
Zra | 0.26 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [55.35; 67.25] | J/mol×K | [297.14; 478.55] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 56 58 60 62 64 66 68 300 350 400 450 | ||||
Cp,gas | 55.35 | J/mol×K | 297.14 | Joback Calculated Property |
Cp,gas | 57.56 | J/mol×K | 327.38 | Joback Calculated Property |
Cp,gas | 59.68 | J/mol×K | 357.61 | Joback Calculated Property |
Cp,gas | 61.71 | J/mol×K | 387.85 | Joback Calculated Property |
Cp,gas | 63.64 | J/mol×K | 418.08 | Joback Calculated Property |
Cp,gas | 65.49 | J/mol×K | 448.32 | Joback Calculated Property |
Cp,gas | 67.25 | J/mol×K | 478.55 | Joback Calculated Property |
Cp,liquid | [100.00; 129.30] | J/mol×K | [292.50; 303.20] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 100 105 110 115 120 125 130 295 300 | ||||
Cp,liquid | 100.80 | J/mol×K | 292.50 | NIST |
Cp,liquid | 100.50 | J/mol×K | 292.50 | NIST |
Cp,liquid | 129.30 | J/mol×K | 298.00 | NIST |
Cp,liquid | 100.00 | J/mol×K | 298.00 | NIST |
Cp,liquid | 100.00 | J/mol×K | 298.10 | NIST |
Cp,liquid | 102.30 | J/mol×K | 298.15 | NIST |
Cp,liquid | 105.50 | J/mol×K | 303.20 | NIST |
η | [0.0003120; 0.0026264] | Pa×s | [160.87; 297.14] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 200 250 300 | ||||
η | 0.0026264 | Pa×s | 160.87 | Joback Calculated Property |
η | 0.0014784 | Pa×s | 183.58 | Joback Calculated Property |
η | 0.0009444 | Pa×s | 206.29 | Joback Calculated Property |
η | 0.0006594 | Pa×s | 229.00 | Joback Calculated Property |
η | 0.0004912 | Pa×s | 251.72 | Joback Calculated Property |
η | 0.0003842 | Pa×s | 274.43 | Joback Calculated Property |
η | 0.0003120 | Pa×s | 297.14 | Joback Calculated Property |
ΔfusH | [6.16; 6.16] | kJ/mol | [178.20; 178.22] | ![]() |
ΔfusH | 6.16 | kJ/mol | 178.20 | NIST |
ΔfusH | 6.16 | kJ/mol | 178.20 | NIST |
ΔfusH | 6.16 | kJ/mol | 178.22 | NIST |
ΔvapH | [28.06; 30.30] | kJ/mol | [249.00; 347.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 28 28.5 29 29.5 30 30.5 250 300 | ||||
ΔvapH | 29.40 | kJ/mol | 249.00 | NIST |
ΔvapH | 30.20 | kJ/mol | 273.00 | NIST |
ΔvapH | 30.30 | kJ/mol | 287.50 | NIST |
ΔvapH | 29.20 | kJ/mol | 308.00 | NIST |
ΔvapH | 28.06 | kJ/mol | 313.00 | NIST |
ΔvapH | 29.00 | kJ/mol | 347.00 | NIST |
Pvap | [34.66; 197.94] | kPa | [285.89; 333.15] | ![]() |
T(K) Vapor pressure (kPa) 50 100 150 200 300 320 | ||||
Pvap | 34.66 | kPa | 285.89 | Limitin... |
Pvap | 37.10 | kPa | 287.00 | Effect ... |
Pvap | 37.33 | kPa | 287.58 | Limitin... |
Pvap | 41.33 | kPa | 289.94 | Limitin... |
Pvap | 45.70 | kPa | 291.90 | Effect ... |
Pvap | 45.33 | kPa | 292.12 | Limitin... |
Pvap | 49.33 | kPa | 294.15 | Limitin... |
Pvap | 53.33 | kPa | 296.05 | Limitin... |
Pvap | 55.90 | kPa | 296.80 | Effect ... |
Pvap | 58.66 | kPa | 298.41 | Limitin... |
Pvap | 63.99 | kPa | 300.61 | Limitin... |
Pvap | 67.40 | kPa | 301.80 | Effect ... |
Pvap | 69.33 | kPa | 302.67 | Limitin... |
Pvap | 70.49 | kPa | 303.15 | Total V... |
Pvap | 74.66 | kPa | 304.61 | Limitin... |
Pvap | 79.99 | kPa | 306.43 | Limitin... |
Pvap | 85.33 | kPa | 308.17 | Limitin... |
Pvap | 90.66 | kPa | 309.82 | Limitin... |
Pvap | 95.99 | kPa | 311.39 | Limitin... |
Pvap | 197.94 | kPa | 333.15 | Vapor L... |
n0 | [1.42190; 1.43050] | [283.15; 298.15] | ![]() |
|
T(K) Refractive Index 1.42 1.42 1.43 1.43 1.43 285 290 295 | ||||
n0 | 1.43050 | 283.15 | Partial... | |
n0 | 1.42760 | 288.15 | Partial... | |
n0 | 1.42370 | 293.15 | Solubil... | |
n0 | 1.42370 | 293.15 | Solubil... | |
n0 | 1.42510 | 293.15 | Partial... | |
n0 | 1.42190 | 298.15 | Partial... | |
ρl | [1307.51; 1334.81] | kg/m3 | [288.15; 303.15] | ![]() |
T(K) Liquid Density (kg/m3) 1305 1310 1315 1320 1325 1330 1335 290 295 300 | ||||
ρl | 1334.81 | kg/m3 | 288.15 | Volumet... |
ρl | 1334.08 | kg/m3 | 288.15 | Volumet... |
ρl | 1325.79 | kg/m3 | 293.15 | Volumet... |
ρl | 1325.67 | kg/m3 | 293.15 | Volumet... |
ρl | 1327.00 | kg/m3 | 293.15 | Interfa... |
ρl | 1317.00 | kg/m3 | 298.00 | KDB |
ρl | 1316.58 | kg/m3 | 298.15 | Volumet... |
ρl | 1316.75 | kg/m3 | 298.15 | Volumet... |
ρl | 1307.51 | kg/m3 | 303.15 | Volumet... |
ρl | 1307.60 | kg/m3 | 303.15 | Viscosi... |
ρl | 1307.90 | kg/m3 | 303.15 | Volumet... |
γ | 0.03 | N/m | 293.20 | KDB |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboil | 313.25 | K | 96.60 | Low cos... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 6037.79] | kPa | [229.18; 510.00] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43555e+01 | |||
Coefficient B | -2.65134e+03 | |||
Coefficient C | -4.07080e+01 | |||
Temperature range, min. | 229.18 | |||
Temperature range, max. | 510.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 | ||||
Pvap | 1.33 | kPa | 229.18 | Calculated Property |
Pvap | 9.84 | kPa | 260.38 | Calculated Property |
Pvap | 44.13 | kPa | 291.58 | Calculated Property |
Pvap | 142.05 | kPa | 322.79 | Calculated Property |
Pvap | 362.24 | kPa | 353.99 | Calculated Property |
Pvap | 779.68 | kPa | 385.19 | Calculated Property |
Pvap | 1477.51 | kPa | 416.39 | Calculated Property |
Pvap | 2538.44 | kPa | 447.60 | Calculated Property |
Pvap | 4037.60 | kPa | 478.80 | Calculated Property |
Pvap | 6037.79 | kPa | 510.00 | Calculated Property |
Pvap | [7.05e-03; 6143.24] | kPa | [178.01; 510.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.08779e+01 | |||
Coefficient B | -6.03061e+03 | |||
Coefficient C | -1.00863e+01 | |||
Coefficient D | 9.81251e-06 | |||
Temperature range, min. | 178.01 | |||
Temperature range, max. | 510.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 200 300 400 500 | ||||
Pvap | 7.05e-03 | kPa | 178.01 | Calculated Property |
Pvap | 0.41 | kPa | 214.90 | Calculated Property |
Pvap | 5.96 | kPa | 251.79 | Calculated Property |
Pvap | 38.97 | kPa | 288.67 | Calculated Property |
Pvap | 154.35 | kPa | 325.56 | Calculated Property |
Pvap | 441.82 | kPa | 362.45 | Calculated Property |
Pvap | 1018.41 | kPa | 399.34 | Calculated Property |
Pvap | 2026.99 | kPa | 436.22 | Calculated Property |
Pvap | 3650.30 | kPa | 473.11 | Calculated Property |
Pvap | 6143.24 | kPa | 510.00 | Calculated Property |
Find more compounds similar to Methylene chloride.
Find more mixtures with Methylene chloride.
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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.