- 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.
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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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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 | |||
| 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 | |||
| 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
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