- InChI
- InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2
- InChI Key
- WSLDOOZREJYCGB-UHFFFAOYSA-N
- Formula
- C2H4Cl2
- SMILES
- ClCCCl
- Molecular Weight1
- 98.96
- CAS
- 107-06-2
- Other Names
-
- 1,2-Bichloroethane
- 1,2-DCE
- 1,2-Dichloorethaan
- 1,2-Dichlor-aethan
- 1,2-Dichlorethane
- 1,2-Dichloroethane
- 1,2-Dicloroetano
- 1,2-Ethylene dichloride
- 1,2-dichloroethane (ethylene dichloride)
- ALPHA,BETA-DICHLOROETHANE
- Aethylenchlorid
- Bichlorure D'ethylene
- Borer sol
- Brocide
- CH2ClCH2Cl
- Chlorure D'ethylene
- Cloruro di ethene
- DCE
- Destruxol borer-sol
- Di-chlor-mulsion
- Dichloremulsion
- Dichloro-1,2-ethane
- Dutch liquid
- Dutch oil
- EDC
- EDC (halocarbon)
- ENT 1,656
- ETHYLENE DICHLORIDE
- Ethane dichloride
- Ethyleendichloride
- Ethylene chloride
- Freon 150
- Glycol dichloride
- HCC 150
- NCI-C00511
- R-150
- Rcra waste number U077
- UN 1184
- s-Dichloroethane
- sym-Dichloroethane
- «alpha»,«beta»-Dichloroethane
- «alpha»,«beta»-Dichloroethane
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2780 | KDB | |
| ΔcH°liquid | [-1246.40; -1236.40] | kJ/mol |
|
| ΔcH°liquid | -1236.40 | kJ/mol | NIST |
| ΔcH°liquid | -1246.40 ± 8.40 | kJ/mol | NIST |
| μ | 1.80 | debye | KDB |
| η | 0.0008270 | Pa×s | Studies... |
| ΔfG° | -73.90 | kJ/mol | KDB |
| Rg | 2.8510 | KDB | |
| ΔfH°gas | [-132.00; -125.40] | kJ/mol |
|
| ΔfH°gas | -129.80 | kJ/mol | KDB |
| ΔfH°gas | -132.00 ± 3.50 | kJ/mol | NIST |
| ΔfH°gas | -125.40 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | -129.00 | kJ/mol | NIST |
| ΔfH°liquid | [-169.70; -167.20] | kJ/mol |
|
| ΔfH°liquid | -167.20 ± 3.50 | kJ/mol | NIST |
| ΔfH°liquid | -169.70 | kJ/mol | NIST |
| ΔfusH° | 9.33 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [34.40; 35.40] | kJ/mol |
|
| ΔvapH° | 35.22 | kJ/mol | NIST |
| ΔvapH° | 35.20 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 35.21 ± 0.05 | kJ/mol | NIST |
| ΔvapH° | Outlier 34.40 | kJ/mol | NIST |
| ΔvapH° | 35.10 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.15 ± 0.01 | kJ/mol | NIST |
| ΔvapH° | 35.40 ± 0.08 | kJ/mol | NIST |
| IE | [11.04; 11.40] | eV |
|
| IE | 11.07 ± 0.04 | eV | NIST |
| IE | 11.05 | eV | NIST |
| IE | 11.04 | eV | NIST |
| IE | 11.12 ± 0.05 | eV | NIST |
| IE | 11.40 ± 0.10 | eV | NIST |
| IE | 11.22 ± 0.02 | eV | NIST |
| IE | 11.39 ± 0.03 | eV | NIST |
| log10WS | [-1.07; -1.06] |
|
|
| log10WS | -1.07 | Aq. Sol... | |
| log10WS | -1.06 | Estimat... | |
| logPoct/wat | 1.464 | Crippen Calculated Property | |
| McVol | 63.520 | ml/mol | McGowan Calculated Property |
| Pc | [5380.00; 5400.00] | kPa |
|
| Pc | 5400.00 | kPa | KDB |
| Pc | 5380.00 ± 50.00 | kPa | NIST |
| ρc | 440.37 ± 14.84 | kg/m3 | NIST |
| Inp | [586.00; 673.00] |
|
|
| Inp | 645.40 | NIST | |
| Inp | 648.20 | NIST | |
| Inp | 656.20 | NIST | |
| Inp | 654.00 | NIST | |
| Inp | 650.10 | NIST | |
| Inp | 647.70 | NIST | |
| Inp | 644.80 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 630.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 633.00 | NIST | |
| Inp | 645.00 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 643.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 628.60 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | Outlier 586.00 | NIST | |
| Inp | Outlier 595.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 633.00 | NIST | |
| Inp | 630.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | Outlier 673.00 | NIST | |
| Inp | 630.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 649.30 | NIST | |
| Inp | 635.50 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 628.60 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | Outlier 595.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 635.50 | NIST | |
| I | [1045.00; 1093.00] |
|
|
| I | 1085.00 | NIST | |
| I | 1090.00 | NIST | |
| I | 1080.00 | NIST | |
| I | 1084.20 | NIST | |
| I | 1084.96 | NIST | |
| I | 1077.64 | NIST | |
| I | 1076.00 | NIST | |
| I | 1072.00 | NIST | |
| I | 1093.00 | NIST | |
| I | 1088.00 | NIST | |
| I | 1088.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1045.00 | NIST | |
| I | 1045.00 | NIST | |
| I | 1051.00 | NIST | |
| I | 1088.00 | NIST | |
| I | 1045.00 | NIST | |
| S°liquid | 208.53 | J/mol×K | NIST |
| Tboil | [356.59; 356.95] | K |
|
| Tboil | 356.60 | K | KDB |
| Tboil | 356.70 | K | Excess ... |
| Tboil | 356.95 | K | Excess ... |
| Tboil | 356.59 | K | Isobari... |
| Tboil | 356.95 | K | Vapor-L... |
| Tboil | 356.95 | K | Isobari... |
| Tc | [561.00; 563.15] | K |
|
| Tc | 561.00 | K | KDB |
| Tc | 561.60 ± 0.40 | K | NIST |
| Tc | 561.20 | K | NIST |
| Tc | 563.15 ± 3.00 | K | NIST |
| Tfus | [176.35; 241.15] | K |
|
| Tfus | 237.60 | K | KDB |
| Tfus | 237.65 | K | Aq. Sol... |
| Tfus | 241.15 ± 1.00 | K | NIST |
| Tfus | 237.45 | K | NIST |
| Tfus | 237.50 ± 0.02 | K | NIST |
| Tfus | 237.85 ± 0.40 | K | NIST |
| Tfus | 237.28 ± 0.05 | K | NIST |
| Tfus | 237.70 ± 0.20 | K | NIST |
| Tfus | Outlier 176.35 ± 0.40 | K | NIST |
| Tfus | 237.65 ± 0.30 | K | NIST |
| Tfus | 237.85 ± 0.30 | K | NIST |
| Tfus | 237.88 ± 0.20 | K | NIST |
| Ttriple | [237.20; 237.60] | K |
|
| Ttriple | 237.60 ± 0.30 | K | NIST |
| Ttriple | 237.20 ± 0.02 | K | NIST |
| Vc | 0.225 | m3/kmol | KDB |
| Zc | 0.2604810 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [81.34; 103.15] | J/mol×K | [320.02; 502.16] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 80 85 90 95 100 105 350 400 450 500 | ||||
| Cp,gas | 81.34 | J/mol×K | 320.02 | Joback Calculated Property |
| Cp,gas | 85.39 | J/mol×K | 350.38 | Joback Calculated Property |
| Cp,gas | 89.27 | J/mol×K | 380.73 | Joback Calculated Property |
| Cp,gas | 92.98 | J/mol×K | 411.09 | Joback Calculated Property |
| Cp,gas | 96.53 | J/mol×K | 441.45 | Joback Calculated Property |
| Cp,gas | 99.91 | J/mol×K | 471.80 | Joback Calculated Property |
| Cp,gas | 103.15 | J/mol×K | 502.16 | Joback Calculated Property |
| Cp,liquid | [122.20; 131.00] | J/mol×K | [293.00; 300.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 122 124 126 128 130 294 296 298 300 | ||||
| Cp,liquid | 129.20 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 124.30 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 123.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 129.70 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 122.20 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 129.54 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 128.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 128.99 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 129.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 128.99 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 128.81 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 128.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 129.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 131.00 | J/mol×K | 300.00 | NIST |
| η | [0.0006269; 0.0008700] | Pa×s | [288.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 6.50e-4 7.00e-4 7.50e-4 8.00e-4 8.50e-4 290 300 310 | ||||
| η | 0.0008700 | Pa×s | 288.15 | Densiti... |
| η | 0.0008112 | Pa×s | 293.15 | Densiti... |
| η | 0.0007902 | Pa×s | 298.15 | Thermop... |
| η | 0.0007597 | Pa×s | 298.15 | Densiti... |
| η | 0.0007291 | Pa×s | 303.15 | Thermop... |
| η | 0.0007112 | Pa×s | 303.15 | Densiti... |
| η | 0.0006739 | Pa×s | 308.15 | Thermop... |
| η | 0.0006747 | Pa×s | 308.15 | Densiti... |
| η | 0.0006441 | Pa×s | 313.15 | Thermop... |
| η | 0.0006269 | Pa×s | 313.15 | Densiti... |
| ΔfusH | [2.85; 8.84] | kJ/mol | [175.00; 237.60] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 3 4 5 6 7 8 9 180 200 220 | ||||
| ΔfusH | 2.85 | kJ/mol | 175.00 | NIST |
| ΔfusH | 8.84 | kJ/mol | 237.20 | NIST |
| ΔfusH | 8.83 | kJ/mol | 237.20 | NIST |
| ΔfusH | 8.83 | kJ/mol | 237.20 | NIST |
| ΔfusH | 8.75 | kJ/mol | 237.60 | NIST |
| ΔvapH | [31.10; 40.80] | kJ/mol | [273.00; 542.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 34 36 38 40 300 400 500 | ||||
| ΔvapH | 33.91 | kJ/mol | 273.00 | NIST |
| ΔvapH | 37.50 | kJ/mol | 307.50 | NIST |
| ΔvapH | 34.80 | kJ/mol | 326.50 | NIST |
| ΔvapH | 34.70 | kJ/mol | 329.00 | NIST |
| ΔvapH | 34.80 | kJ/mol | 356.50 | NIST |
| ΔvapH | 31.98 | kJ/mol | 356.60 | NIST |
| ΔvapH | 32.01 | kJ/mol | 357.10 | KDB |
| ΔvapH | 31.10 | kJ/mol | 446.00 | NIST |
| ΔvapH | 31.10 | kJ/mol | 457.00 | NIST |
| ΔvapH | 40.80 | kJ/mol | 542.00 | NIST |
| Pvap | [5.37; 101.30] | kPa | [284.86; 356.59] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 320 340 | ||||
| Pvap | 5.38 | kPa | 284.86 | Isother... |
| Pvap | 5.37 | kPa | 284.87 | Isother... |
| Pvap | 8.96 | kPa | 294.83 | Isother... |
| Pvap | 8.95 | kPa | 294.84 | Isother... |
| Pvap | 20.75 | kPa | 298.15 | Excess ... |
| Pvap | 13.28 | kPa | 303.15 | Phase E... |
| Pvap | 14.33 | kPa | 304.82 | Isother... |
| Pvap | 14.32 | kPa | 304.82 | Isother... |
| Pvap | 21.05 | kPa | 313.15 | Isother... |
| Pvap | 20.75 | kPa | 313.15 | Excess ... |
| Pvap | 22.18 | kPa | 314.81 | Isother... |
| Pvap | 22.18 | kPa | 314.83 | Isother... |
| Pvap | 33.28 | kPa | 324.82 | Isother... |
| Pvap | 33.27 | kPa | 324.83 | Isother... |
| Pvap | 48.45 | kPa | 334.79 | Isother... |
| Pvap | 48.46 | kPa | 334.82 | Isother... |
| Pvap | 67.97 | kPa | 344.81 | Isother... |
| Pvap | 67.97 | kPa | 344.81 | Isother... |
| Pvap | 67.98 | kPa | 344.82 | Isother... |
| Pvap | 67.98 | kPa | 344.82 | Isother... |
| Pvap | 90.90 | kPa | 353.15 | Phase E... |
| Pvap | 94.94 | kPa | 354.89 | Isother... |
| Pvap | 94.95 | kPa | 354.89 | Isother... |
| Pvap | 94.94 | kPa | 354.89 | Isother... |
| Pvap | 94.95 | kPa | 354.89 | Isother... |
| Pvap | 95.50 | kPa | 355.15 | Vapor-l... |
| Pvap | 101.30 | kPa | 356.59 | Isobari... |
| n0 | [1.41960; 1.44480] | [293.15; 298.15] |
|
|
|
T(K) Refractive Index 1.42 1.43 1.43 1.44 1.44 1.45 294 296 298 | ||||
| n0 | 1.41960 | 293.15 | Bubble ... | |
| n0 | 1.44480 | 293.15 | Excess ... | |
| n0 | 1.41960 | 293.15 | Vapor-L... | |
| n0 | 1.41960 | 293.15 | Bubble ... | |
| n0 | 1.44450 | 293.15 | Isobari... | |
| n0 | 1.41960 | 293.15 | Activit... | |
| n0 | 1.44210 | 298.15 | Vapour ... | |
| n0 | 1.44200 | 298.15 | Thermod... | |
| n0 | 1.44210 | 298.15 | Bubble ... | |
| n0 | 1.44210 | 298.15 | Bubble-... | |
| n0 | 1.44210 | 298.15 | Isother... | |
| ρl | [1193.61; 1267.39] | kg/m3 | [283.15; 333.15] |
|
|
T(K) Liquid Density (kg/m3) 1200 1220 1240 1260 300 320 | ||||
| ρl | 1267.39 | kg/m3 | 283.15 | Volumet... |
| ρl | 1265.95 | kg/m3 | 284.15 | Volumet... |
| ρl | 1264.50 | kg/m3 | 285.15 | Volumet... |
| ρl | 1263.05 | kg/m3 | 286.15 | Volumet... |
| ρl | 1261.60 | kg/m3 | 287.15 | Volumet... |
| ρl | 1260.33 | kg/m3 | 288.15 | Densiti... |
| ρl | 1260.35 | kg/m3 | 288.15 | Densiti... |
| ρl | 1259.99 | kg/m3 | 288.15 | Volumet... |
| ρl | 1260.15 | kg/m3 | 288.15 | Volumet... |
| ρl | 1260.01 | kg/m3 | 288.15 | Densiti... |
| ρl | 1259.99 | kg/m3 | 288.15 | Volumet... |
| ρl | 1250.00 | kg/m3 | 289.00 | KDB |
| ρl | 1258.70 | kg/m3 | 289.15 | Volumet... |
| ρl | 1257.25 | kg/m3 | 290.15 | Volumet... |
| ρl | 1255.80 | kg/m3 | 291.15 | Volumet... |
| ρl | 1254.35 | kg/m3 | 292.15 | Volumet... |
| ρl | 1253.00 | kg/m3 | 293.15 | Influen... |
| ρl | 1252.77 | kg/m3 | 293.15 | Volumet... |
| ρl | 1252.89 | kg/m3 | 293.15 | Volumet... |
| ρl | 1252.82 | kg/m3 | 293.15 | Theoret... |
| ρl | 1252.74 | kg/m3 | 293.15 | Thermop... |
| ρl | 1252.77 | kg/m3 | 293.15 | Volumet... |
| ρl | 1252.15 | kg/m3 | 293.20 | Isobari... |
| ρl | 1251.44 | kg/m3 | 294.15 | Volumet... |
| ρl | 1249.98 | kg/m3 | 295.15 | Volumet... |
| ρl | 1248.52 | kg/m3 | 296.15 | Volumet... |
| ρl | 1247.07 | kg/m3 | 297.15 | Volumet... |
| ρl | 1246.70 | kg/m3 | 298.15 | Excess ... |
| ρl | 1245.68 | kg/m3 | 298.15 | Isother... |
| ρl | 1245.48 | kg/m3 | 298.15 | Densiti... |
| ρl | 1245.75 | kg/m3 | 298.15 | Densiti... |
| ρl | 1245.49 | kg/m3 | 298.15 | Volumet... |
| ρl | 1245.49 | kg/m3 | 298.15 | Volumet... |
| ρl | 1245.76 | kg/m3 | 298.15 | Densiti... |
| ρl | 1245.59 | kg/m3 | 298.15 | Volumet... |
| ρl | 1246.34 | kg/m3 | 298.15 | (Vapor ... |
| ρl | 1245.80 | kg/m3 | 298.15 | Densiti... |
| ρl | 1246.37 | kg/m3 | 298.15 | Hydroge... |
| ρl | 1245.61 | kg/m3 | 298.15 | Volumet... |
| ρl | 1246.00 | kg/m3 | 298.15 | Influen... |
| ρl | 1244.15 | kg/m3 | 299.15 | Volumet... |
| ρl | 1242.69 | kg/m3 | 300.15 | Volumet... |
| ρl | 1241.22 | kg/m3 | 301.15 | Volumet... |
| ρl | 1239.76 | kg/m3 | 302.15 | Volumet... |
| ρl | 1238.70 | kg/m3 | 303.15 | Excess ... |
| ρl | 1238.29 | kg/m3 | 303.15 | Volumet... |
| ρl | 1238.18 | kg/m3 | 303.15 | Volumet... |
| ρl | 1238.00 | kg/m3 | 303.15 | Influen... |
| ρl | 1238.18 | kg/m3 | 303.15 | Volumet... |
| ρl | 1238.27 | kg/m3 | 303.15 | Theoret... |
| ρl | 1236.83 | kg/m3 | 304.15 | Volumet... |
| ρl | 1235.36 | kg/m3 | 305.15 | Volumet... |
| ρl | 1233.89 | kg/m3 | 306.15 | Volumet... |
| ρl | 1232.42 | kg/m3 | 307.15 | Volumet... |
| ρl | 1230.84 | kg/m3 | 308.15 | Volumet... |
| ρl | 1230.83 | kg/m3 | 308.15 | Densiti... |
| ρl | 1231.16 | kg/m3 | 308.15 | Densiti... |
| ρl | 1231.00 | kg/m3 | 308.15 | Influen... |
| ρl | 1230.84 | kg/m3 | 308.15 | Volumet... |
| ρl | 1230.95 | kg/m3 | 308.15 | Volumet... |
| ρl | 1230.50 | kg/m3 | 308.15 | Excess ... |
| ρl | 1230.96 | kg/m3 | 308.15 | Volumet... |
| ρl | 1231.21 | kg/m3 | 308.15 | Hydroge... |
| ρl | 1231.15 | kg/m3 | 308.15 | Densiti... |
| ρl | 1229.47 | kg/m3 | 309.15 | Volumet... |
| ρl | 1228.00 | kg/m3 | 310.15 | Volumet... |
| ρl | 1226.53 | kg/m3 | 311.15 | Volumet... |
| ρl | 1225.05 | kg/m3 | 312.15 | Volumet... |
| ρl | 1223.46 | kg/m3 | 313.15 | Volumet... |
| ρl | 1223.46 | kg/m3 | 313.15 | Volumet... |
| ρl | 1223.70 | kg/m3 | 313.15 | Excess ... |
| ρl | 1223.53 | kg/m3 | 313.15 | Theoret... |
| ρl | 1223.57 | kg/m3 | 313.15 | Volumet... |
| ρl | 1222.09 | kg/m3 | 314.15 | Volumet... |
| ρl | 1220.61 | kg/m3 | 315.15 | Volumet... |
| ρl | 1219.13 | kg/m3 | 316.15 | Volumet... |
| ρl | 1217.64 | kg/m3 | 317.15 | Volumet... |
| ρl | 1216.56 | kg/m3 | 318.15 | Densiti... |
| ρl | 1216.04 | kg/m3 | 318.15 | Densiti... |
| ρl | 1216.16 | kg/m3 | 318.15 | Volumet... |
| ρl | 1216.16 | kg/m3 | 318.15 | Volumet... |
| ρl | 1214.55 | kg/m3 | 318.15 | Hydroge... |
| ρl | 1216.35 | kg/m3 | 318.15 | Densiti... |
| ρl | 1214.67 | kg/m3 | 319.15 | Volumet... |
| ρl | 1213.18 | kg/m3 | 320.15 | Volumet... |
| ρl | 1211.69 | kg/m3 | 321.15 | Volumet... |
| ρl | 1210.20 | kg/m3 | 322.15 | Volumet... |
| ρl | 1208.70 | kg/m3 | 323.15 | Volumet... |
| ρl | 1208.61 | kg/m3 | 323.15 | Theoret... |
| ρl | 1207.21 | kg/m3 | 324.15 | Volumet... |
| ρl | 1205.71 | kg/m3 | 325.15 | Volumet... |
| ρl | 1204.21 | kg/m3 | 326.15 | Volumet... |
| ρl | 1202.71 | kg/m3 | 327.15 | Volumet... |
| ρl | 1201.21 | kg/m3 | 328.15 | Volumet... |
| ρl | 1199.70 | kg/m3 | 329.15 | Volumet... |
| ρl | 1198.19 | kg/m3 | 330.15 | Volumet... |
| ρl | 1196.69 | kg/m3 | 331.15 | Volumet... |
| ρl | 1195.18 | kg/m3 | 332.15 | Volumet... |
| ρl | 1193.61 | kg/m3 | 333.15 | Theoret... |
| ρl | 1193.66 | kg/m3 | 333.15 | Volumet... |
| ΔfusS | [16.20; 37.25] | J/mol×K | [175.00; 237.20] |
|
| ΔfusS | 36.80 | J/mol×K | 175.00 | NIST |
| ΔfusS | 37.25 | J/mol×K | 237.20 | NIST |
| ΔfusS | 16.20 | J/mol×K | 237.20 | NIST |
| csound,fluid | [1117.75; 1212.92] | m/s | [293.15; 318.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1120 1140 1160 1180 1200 1220 300 310 | ||||
| csound,fluid | 1212.92 | m/s | 293.15 | Densiti... |
| csound,fluid | 1193.60 | m/s | 298.15 | Densiti... |
| csound,fluid | 1194.44 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1156.06 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1117.75 | m/s | 318.15 | Speeds ... |
| γ | [0.03; 0.03] | N/m | [293.15; 313.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 295 300 305 310 | ||||
| γ | 0.03 | N/m | 293.15 | The add... |
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 298.15 | The add... |
| γ | 0.03 | N/m | 303.15 | The add... |
| γ | 0.03 | N/m | 308.15 | The add... |
| γ | 0.03 | N/m | 313.15 | The add... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [340.45; 357.25] | K | [60.01; 101.35] |
|
|
P(kPa) Boiling point at given pressure (K) 340 345 350 355 60 80 100 | ||||
| Tboil | 340.45 | K | 60.01 | Isobari... |
| Tboil | 343.85 | K | 66.68 | Isobari... |
| Tboil | 346.55 | K | 73.35 | Isobari... |
| Tboil | 349.45 | K | 80.02 | Isobari... |
| Tboil | 352.05 | K | 86.69 | Isobari... |
| Tboil | 357.25 | K | 101.35 | Isobari... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 308.15 | 101.00 | 0.0006 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 1259.9 |
| 288.15 | 500.00 | 1260.3 |
| 288.15 | 1000.00 | 1260.8 |
| 288.15 | 1500.00 | 1261.2 |
| 288.15 | 2000.00 | 1261.6 |
| 288.15 | 2500.00 | 1262.2 |
| 288.15 | 3100.00 | 1262.7 |
| 288.15 | 3600.00 | 1263.2 |
| 288.15 | 4100.00 | 1263.6 |
| 288.15 | 4600.00 | 1264.0 |
| 288.15 | 5100.00 | 1264.5 |
| 288.15 | 5600.00 | 1264.9 |
| 288.15 | 6100.00 | 1265.4 |
| 288.15 | 6600.00 | 1265.8 |
| 288.15 | 7100.00 | 1266.2 |
| 288.15 | 7600.00 | 1266.7 |
| 288.15 | 8100.00 | 1267.2 |
| 288.15 | 8600.00 | 1267.6 |
| 288.15 | 9200.00 | 1268.2 |
| 288.15 | 9600.00 | 1268.6 |
| 288.15 | 10100.00 | 1269.0 |
| 288.15 | 10600.00 | 1269.4 |
| 288.15 | 11100.00 | 1269.8 |
| 288.15 | 11600.00 | 1270.3 |
| 288.15 | 12100.00 | 1270.7 |
| 288.15 | 12600.00 | 1271.0 |
| 288.15 | 13100.00 | 1271.5 |
| 288.15 | 13600.00 | 1271.9 |
| 288.15 | 14100.00 | 1272.4 |
| 288.15 | 14700.00 | 1272.9 |
| 288.15 | 15200.00 | 1273.3 |
| 288.15 | 15700.00 | 1273.7 |
| 288.15 | 16300.00 | 1274.2 |
| 288.15 | 16800.00 | 1274.6 |
| 288.15 | 17200.00 | 1275.0 |
| 288.15 | 17700.00 | 1275.4 |
| 288.15 | 18200.00 | 1275.8 |
| 288.15 | 18600.00 | 1276.2 |
| 288.15 | 19000.00 | 1276.5 |
| 288.15 | 19400.00 | 1276.9 |
| 288.15 | 20000.00 | 1277.3 |
| 298.15 | 100.00 | 1245.5 |
| 298.15 | 500.00 | 1246.1 |
| 298.15 | 1000.00 | 1246.4 |
| 298.15 | 1500.00 | 1246.9 |
| 298.15 | 2000.00 | 1247.4 |
| 298.15 | 2500.00 | 1247.8 |
| 298.15 | 3100.00 | 1248.5 |
| 298.15 | 3600.00 | 1248.9 |
| 298.15 | 4100.00 | 1249.4 |
| 298.15 | 4600.00 | 1249.9 |
| 298.15 | 5100.00 | 1250.4 |
| 298.15 | 5600.00 | 1250.9 |
| 298.15 | 6100.00 | 1251.4 |
| 298.15 | 6600.00 | 1251.9 |
| 298.15 | 7100.00 | 1252.3 |
| 298.15 | 7600.00 | 1252.9 |
| 298.15 | 8100.00 | 1253.2 |
| 298.15 | 8600.00 | 1253.8 |
| 298.15 | 9200.00 | 1254.4 |
| 298.15 | 9600.00 | 1254.9 |
| 298.15 | 10000.00 | 1255.1 |
| 298.15 | 10600.00 | 1255.9 |
| 298.15 | 11100.00 | 1256.4 |
| 298.15 | 11600.00 | 1256.7 |
| 298.15 | 12100.00 | 1257.3 |
| 298.15 | 12600.00 | 1257.6 |
| 298.15 | 13100.00 | 1258.0 |
| 298.15 | 13600.00 | 1258.5 |
| 298.15 | 14200.00 | 1259.0 |
| 298.15 | 14700.00 | 1259.4 |
| 298.15 | 15200.00 | 1260.0 |
| 298.15 | 15700.00 | 1260.5 |
| 298.15 | 16200.00 | 1260.8 |
| 298.15 | 16700.00 | 1261.4 |
| 298.15 | 17300.00 | 1261.9 |
| 298.15 | 17800.00 | 1262.4 |
| 298.15 | 18300.00 | 1262.8 |
| 298.15 | 18800.00 | 1263.3 |
| 298.15 | 19200.00 | 1263.7 |
| 298.15 | 19700.00 | 1264.1 |
| 298.15 | 20200.00 | 1264.5 |
| 308.15 | 100.00 | 1231.0 |
| 308.15 | 500.00 | 1231.4 |
| 308.15 | 1000.00 | 1232.0 |
| 308.15 | 1500.00 | 1232.5 |
| 308.15 | 2000.00 | 1233.0 |
| 308.15 | 2500.00 | 1233.5 |
| 308.15 | 3100.00 | 1234.2 |
| 308.15 | 3600.00 | 1234.7 |
| 308.15 | 4100.00 | 1235.2 |
| 308.15 | 4600.00 | 1235.7 |
| 308.15 | 5100.00 | 1236.2 |
| 308.15 | 5600.00 | 1236.9 |
| 308.15 | 6100.00 | 1237.3 |
| 308.15 | 6600.00 | 1237.9 |
| 308.15 | 7100.00 | 1238.4 |
| 308.15 | 7600.00 | 1238.6 |
| 308.15 | 8100.00 | 1239.3 |
| 308.15 | 8600.00 | 1239.8 |
| 308.15 | 9200.00 | 1240.4 |
| 308.15 | 9600.00 | 1240.9 |
| 308.15 | 10100.00 | 1241.3 |
| 308.15 | 10600.00 | 1241.8 |
| 308.15 | 11100.00 | 1242.3 |
| 308.15 | 11600.00 | 1242.8 |
| 308.15 | 12100.00 | 1243.4 |
| 308.15 | 12600.00 | 1243.8 |
| 308.15 | 13100.00 | 1244.2 |
| 308.15 | 13600.00 | 1244.7 |
| 308.15 | 14200.00 | 1245.3 |
| 308.15 | 14700.00 | 1245.8 |
| 308.15 | 15200.00 | 1246.4 |
| 308.15 | 15700.00 | 1246.8 |
| 308.15 | 16200.00 | 1247.2 |
| 308.15 | 16700.00 | 1247.7 |
| 308.15 | 17200.00 | 1248.2 |
| 308.15 | 17800.00 | 1248.7 |
| 308.15 | 18300.00 | 1249.2 |
| 308.15 | 18800.00 | 1249.6 |
| 308.15 | 19200.00 | 1250.1 |
| 308.15 | 19700.00 | 1250.6 |
| 308.15 | 20200.00 | 1251.0 |
| 318.15 | 100.00 | 1216.4 |
| 318.15 | 500.00 | 1216.7 |
| 318.15 | 1000.00 | 1217.4 |
| 318.15 | 1500.00 | 1218.0 |
| 318.15 | 2000.00 | 1218.5 |
| 318.15 | 2500.00 | 1219.1 |
| 318.15 | 3100.00 | 1219.8 |
| 318.15 | 3600.00 | 1220.3 |
| 318.15 | 4100.00 | 1220.9 |
| 318.15 | 4600.00 | 1221.4 |
| 318.15 | 5100.00 | 1222.0 |
| 318.15 | 5600.00 | 1222.6 |
| 318.15 | 6100.00 | 1223.1 |
| 318.15 | 6600.00 | 1223.6 |
| 318.15 | 7100.00 | 1224.1 |
| 318.15 | 7600.00 | 1224.7 |
| 318.15 | 8100.00 | 1225.2 |
| 318.15 | 8600.00 | 1225.8 |
| 318.15 | 9200.00 | 1226.3 |
| 318.15 | 9600.00 | 1226.9 |
| 318.15 | 10100.00 | 1227.5 |
| 318.15 | 10600.00 | 1227.9 |
| 318.15 | 11100.00 | 1228.4 |
| 318.15 | 11600.00 | 1229.0 |
| 318.15 | 12100.00 | 1229.5 |
| 318.15 | 12500.00 | 1230.0 |
| 318.15 | 13100.00 | 1230.6 |
| 318.15 | 13600.00 | 1231.0 |
| 318.15 | 14200.00 | 1231.6 |
| 318.15 | 14700.00 | 1232.1 |
| 318.15 | 15200.00 | 1232.7 |
| 318.15 | 15600.00 | 1233.1 |
| 318.15 | 16300.00 | 1233.8 |
| 318.15 | 16800.00 | 1234.2 |
| 318.15 | 17300.00 | 1234.8 |
| 318.15 | 17800.00 | 1235.2 |
| 318.15 | 18200.00 | 1235.5 |
| 318.15 | 18900.00 | 1236.2 |
| 318.15 | 19200.00 | 1236.5 |
| 318.15 | 19700.00 | 1237.1 |
| 318.15 | 20200.00 | 1237.5 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.24; 5372.05] | kPa | [237.49; 561.60] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47712e+01 | |||
| Coefficient B | -3.23907e+03 | |||
| Coefficient C | -3.76700e+01 | |||
| Temperature range, min. | 237.49 | |||
| Temperature range, max. | 561.60 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
| Pvap | 0.24 | kPa | 237.49 | Calculated Property |
| Pvap | 2.82 | kPa | 273.50 | Calculated Property |
| Pvap | 17.39 | kPa | 309.51 | Calculated Property |
| Pvap | 70.10 | kPa | 345.53 | Calculated Property |
| Pvap | 210.97 | kPa | 381.54 | Calculated Property |
| Pvap | 515.27 | kPa | 417.55 | Calculated Property |
| Pvap | 1078.15 | kPa | 453.56 | Calculated Property |
| Pvap | 2005.48 | kPa | 489.58 | Calculated Property |
| Pvap | 3403.86 | kPa | 525.59 | Calculated Property |
| Pvap | 5372.05 | kPa | 561.60 | Calculated Property |
| Pvap | [0.24; 5298.45] | kPa | [237.49; 561.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.39680e+01 | |||
| Coefficient B | -6.90490e+03 | |||
| Coefficient C | -1.03825e+01 | |||
| Coefficient D | 8.36813e-06 | |||
| Temperature range, min. | 237.49 | |||
| Temperature range, max. | 561.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
| Pvap | 0.24 | kPa | 237.49 | Calculated Property |
| Pvap | 2.96 | kPa | 273.44 | Calculated Property |
| Pvap | 18.38 | kPa | 309.38 | Calculated Property |
| Pvap | 72.99 | kPa | 345.33 | Calculated Property |
| Pvap | 213.97 | kPa | 381.27 | Calculated Property |
| Pvap | 508.21 | kPa | 417.22 | Calculated Property |
| Pvap | 1040.46 | kPa | 453.16 | Calculated Property |
| Pvap | 1916.26 | kPa | 489.11 | Calculated Property |
| Pvap | 3272.72 | kPa | 525.05 | Calculated Property |
| Pvap | 5298.45 | kPa | 561.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1,2-dichloro-.
Mixtures
- Ethyl Acetate + Ethane, 1,2-dichloro-
- Ethane, 1,2-dichloro- + 1-Hexanol
- Phenol, 2-methyl- + Ethane, 1,2-dichloro-
- Ethane, 1,2-dibromo- + Ethane, 1,2-dichloro-
- Formamide, N,N-dimethyl- + Ethane, 1,2-dichloro-
- Cyclohexanone + Ethane, 1,2-dichloro-
- Ethyl ether + Ethane, 1,2-dichloro-
- Diisopropyl ether + Ethane, 1,2-dichloro-
- Propane, 2-methoxy-2-methyl- + Ethane, 1,2-dichloro-
- 2-Propenenitrile + Ethane, 1,2-dichloro-
- Ethane, 1,2-dichloro- + Methane, nitro-
- Ethane, 1,2-dichloro- + Phosphoramidic acid, phenyl-, diphenyl ester
- Ethane, 1,2-dichloro- + 1,4-Dioxane
- 1-Propanol + Ethane, 1,2-dichloro-
- Butanoic acid, ethyl ester + Ethane, 1,2-dichloro-
- Pentanoic acid, ethyl ester + Ethane, 1,2-dichloro-
- Ethyl formate + Ethane, 1,2-dichloro-
- Propanoic acid, ethyl ester + Ethane, 1,2-dichloro-
- Ethane, 1,2-dichloro- + Cyclopentanone
- Formic acid, butyl ester + Ethane, 1,2-dichloro-
Find more mixtures with Ethane, 1,2-dichloro-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Temperature and Pressure Dependence of the Volumetric Properties of Binary Liquid Mixtures Containing Dihaloalkanes
- Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
- Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
- Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
- Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
- Co-solvent effects in LLE of 1-hydroxyethyl-3-methylimidazolium based ionic liquids + 2-propanol + dichloromethane or 1,2-dichloroethane
- A simple apparatus for data solubility determination
- Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
- Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
- Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
- Isothermal vapour liquid equilibria for 1,2-dichloroethane + nitromethane and + nitroethane binary systems at temperatures between 333.15 and 353.15K
- Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
- Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
- Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
- Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
- Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- (Vapor + liquid) equilibria for the binary mixtures (1-propanol + dibromomethane, or + bromochloromethane, or + 1,2-dichloroethane or +1-bromo-2-chloroethane) at T = 313.15 K.
- Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
- Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
- Densities and viscosities of binary liquid mixtures of N-methylacetamide with some chloroethanes and chloroethenes at T = 308.15 K
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) V. Hex and Vex for 25 binary mixtures {xCu-1H2u-1CO2CH3 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
- Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
- Excess molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
- Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) VII. HE m and VE m for 20 binary mixtures {xCu 1H2u 1CO2C3H7 + (1 x)a,x-ClCH2(CH2)v 2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6. An analysis of behavior using the COSMO-RS methodology
- Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
- Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
- (Liquid + liquid) equilibria of quaternary systems containing water, phosphoric acid, dichloromethane and 1,2-dichloroethane
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Salting-out effect on the (liquid + liquid) equilibrium for the ternary systems (water + phosphoric acid + dichloromethane or 1,2-dichloroethane)
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
- Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
- Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
- Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
- Volumetric and electromagnetic properties of binary mixtures consist of benzene derivatives at different temperature and ternary mixtures with 1,2-dichloroethane at T = 293.15 K with application of the Prigogine-Flory-Patterson theory and PC-SAFT
- Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
- Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
- Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
- Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
- Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Solution Thermodynamics of Benzotriazole in Different Pure Solvents
- Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
- Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
- Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 1,2-Dichloroethane + sec-Butyl Acetate, n-Propyl Acetate, and tert-Butyl Acetate at 101.3 kPa
- Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
- Measurement and Correlation of Solubilities of 5,5'-Dinitramino-3,3'-bi[1,2,4-triazolate] Carbohydrazide Salt (CBNT) in Various Pure Solvents and a Binary Mixture (Dimethyl Sulfoxide + Water) from 298.15 to 343.15 K
- Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
- Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
- Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
- Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
- Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
- Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
- Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 313.15 K
- Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
- Solubilities of 2,4-Dinitro-l-phenylalanine in Monosolvents at (273.15 to 368.15) K
- Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
- Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Measurement and Correlation of the Solubility of Prednisone Acetate in Different Solvents
- Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
- Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
- Determination of Gas Concentrations in Liquids by Nuclear Magnetic Resonance: Hydrogen in Organic Solvents
- Solubilities of 3-Methoxy-N-phenylaniline and 3-(Methylthio)-N-phenylaniline in Five Organic Solvents (285 K to 333.75 K)
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
- Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,a-5,5-tetramethyl 2-oxide in Selected Solvents at 273.15 K to 343.15 K
- Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,5,5-trimethyl-a-phenyl-2-oxide in Selected Solvents between 278.15 K and 343.15 K
- Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + r,o-Dichloroalkane
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
- Solubility of Imidacloprid in Different Solvents
- Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
- Solubility of Enrofloxacin Sodium in Various Solvents at Various Temperatures
- Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
- Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
- Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
- Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
- Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) K
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.