- InChI
- InChI=1S/C2H2Cl4/c3-1(4)2(5)6/h1-2H
- InChI Key
- QPFMBZIOSGYJDE-UHFFFAOYSA-N
- Formula
- C2H2Cl4
- SMILES
- ClC(Cl)C(Cl)Cl
- Molecular Weight1
- 167.85
- CAS
- 79-34-5
- Other Names
-
- (CHCl2)2
- 1,1,2,2-Czterochloroetan
- 1,1,2,2-TETRACHLOROETHANE
- 1,1,2,2-Tetrachloorethaan
- 1,1,2,2-Tetrachloraethan
- 1,1,2,2-Tetrachlorethane
- 1,1,2,2-Tetracloroetano
- 1,1-Dichloro-2,2-dichloroethane
- ACETYLENE TETRACHLORIDE
- Acetosol
- Bonoform
- Cellon
- Freon 130
- NCI-C03554
- NSC 60912
- R-130
- Rcra waste number U209
- S-TETRACHLOROETHANE
- Tetrachlorethane
- Tetrachloroethane
- Tetrachlorure d'acetylene
- UN 1702
- Westron
- sym-Tetrachloroethane
- 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).
- 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.
- 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).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -972.80 ± 8.40 | kJ/mol | NIST |
| μ | 1.50 | debye | KDB |
| ΔfG° | -85.83 | kJ/mol | KDB |
| ΔfH°gas | [-156.70; -152.80] | kJ/mol |
|
| ΔfH°gas | -152.80 | kJ/mol | KDB |
| ΔfH°gas | -156.70 ± 3.50 | kJ/mol | NIST |
| ΔfH°gas | -155.60 ± 8.40 | kJ/mol | NIST |
| ΔfH°liquid | [-202.40; -195.40] | kJ/mol |
|
| ΔfH°liquid | -202.40 ± 3.50 | kJ/mol | NIST |
| ΔfH°liquid | -195.40 ± 8.40 | kJ/mol | NIST |
| ΔfusH° | 10.68 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [45.20; 45.80] | kJ/mol |
|
| ΔvapH° | 45.72 | kJ/mol | NIST |
| ΔvapH° | 45.73 ± 0.09 | kJ/mol | NIST |
| ΔvapH° | 45.78 ± 0.16 | kJ/mol | NIST |
| ΔvapH° | 45.80 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 45.20 ± 1.30 | kJ/mol | NIST |
| IE | [11.10; 11.62] | eV |
|
| IE | 11.62 | eV | NIST |
| IE | 11.10 ± 0.05 | eV | NIST |
| log10WS | [-1.74; -1.74] |
|
|
| log10WS | -1.74 | Aq. Sol... | |
| log10WS | -1.74 | Estimat... | |
| logPoct/wat | 2.594 | Crippen Calculated Property | |
| McVol | 88.000 | ml/mol | McGowan Calculated Property |
| Pc | 5840.00 | kPa | KDB |
| Inp | [865.00; 922.10] |
|
|
| Inp | 888.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | Outlier 922.10 | NIST | |
| Inp | 888.40 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 876.00 | NIST | |
| I | [1475.00; 1555.00] |
|
|
| I | 1513.66 | NIST | |
| I | 1515.59 | NIST | |
| I | 1511.30 | NIST | |
| I | 1516.00 | NIST | |
| I | Outlier 1555.00 | NIST | |
| I | 1516.00 | NIST | |
| I | 1475.00 | NIST | |
| I | 1475.00 | NIST | |
| I | 1500.00 | NIST | |
| S°liquid | [244.30; 247.00] | J/mol×K |
|
| S°liquid | 244.30 | J/mol×K | NIST |
| S°liquid | 247.00 | J/mol×K | NIST |
| Tboil | [418.35; 419.60] | K |
|
| Tboil | 419.60 | K | KDB |
| Tboil | 419.25 | K | Excess ... |
| Tboil | 418.35 | K | Excess ... |
| Tboil | 419.35 | K | Vapor-L... |
| Tboil | 418.35 | K | Isobari... |
| Tc | [644.50; 661.15] | K |
|
| Tc | 661.15 | K | KDB |
| Tc | 644.50 | K | NIST |
| Tfus | [229.30; 229.70] | K |
|
| Tfus | 229.30 | K | KDB |
| Tfus | 229.70 | K | Aq. Sol... |
| Tfus | 229.70 ± 0.60 | K | NIST |
| Ttriple | [230.30; 230.80] | K |
|
| Ttriple | 230.80 ± 0.20 | K | NIST |
| Ttriple | 230.30 ± 0.20 | K | NIST |
| Vc | 0.332 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [117.05; 137.38] | J/mol×K | [394.00; 605.61] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 120 125 130 135 400 500 600 | ||||
| Cp,gas | 117.05 | J/mol×K | 394.00 | Joback Calculated Property |
| Cp,gas | 121.09 | J/mol×K | 429.27 | Joback Calculated Property |
| Cp,gas | 124.85 | J/mol×K | 464.54 | Joback Calculated Property |
| Cp,gas | 128.35 | J/mol×K | 499.80 | Joback Calculated Property |
| Cp,gas | 131.60 | J/mol×K | 535.07 | Joback Calculated Property |
| Cp,gas | 134.60 | J/mol×K | 570.34 | Joback Calculated Property |
| Cp,gas | 137.38 | J/mol×K | 605.61 | Joback Calculated Property |
| Cp,liquid | [165.30; 168.00] | J/mol×K | [298.00; 298.15] |
|
| Cp,liquid | 165.30 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 168.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 165.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 165.40 | J/mol×K | 298.15 | NIST |
| η | [0.0004249; 0.0088772] | Pa×s | [201.98; 394.00] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 200 250 300 350 | ||||
| η | 0.0088772 | Pa×s | 201.98 | Joback Calculated Property |
| η | 0.0037828 | Pa×s | 233.98 | Joback Calculated Property |
| η | 0.0019792 | Pa×s | 265.99 | Joback Calculated Property |
| η | 0.0011902 | Pa×s | 297.99 | Joback Calculated Property |
| η | 0.0007899 | Pa×s | 329.99 | Joback Calculated Property |
| η | 0.0005636 | Pa×s | 362.00 | Joback Calculated Property |
| η | 0.0004249 | Pa×s | 394.00 | Joback Calculated Property |
| ΔfusH | [0.36; 9.52] | kJ/mol | [204.80; 230.80] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0 2 4 6 8 10 210 220 230 | ||||
| ΔfusH | 0.36 | kJ/mol | 204.80 | NIST |
| ΔfusH | 0.54 | kJ/mol | 207.30 | NIST |
| ΔfusH | 9.52 | kJ/mol | 230.30 | NIST |
| ΔfusH | 9.17 | kJ/mol | 230.80 | NIST |
| ΔfusH | 9.17 | kJ/mol | 230.80 | NIST |
| ΔvapH | [37.64; 47.70] | kJ/mol | [350.50; 419.40] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 38 40 42 44 46 48 360 380 400 420 | ||||
| ΔvapH | 47.70 | kJ/mol | 350.50 | NIST |
| ΔvapH | 45.70 | kJ/mol | 361.50 | NIST |
| ΔvapH | 42.50 | kJ/mol | 380.50 | NIST |
| ΔvapH | 40.80 | kJ/mol | 395.00 | NIST |
| ΔvapH | 41.90 | kJ/mol | 396.00 | NIST |
| ΔvapH | 40.10 | kJ/mol | 397.50 | NIST |
| ΔvapH | 40.40 | kJ/mol | 398.00 | NIST |
| ΔvapH | 39.00 | kJ/mol | 415.00 | NIST |
| ΔvapH | 41.49 | kJ/mol | 419.20 | KDB |
| ΔvapH | 37.64 | kJ/mol | 419.40 | NIST |
| Pvap | [0.26; 95.50] | kPa | [283.15; 417.25] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.26 | kPa | 283.15 | Isother... |
| Pvap | 0.26 | kPa | 283.15 | Total v... |
| Pvap | 0.26 | kPa | 283.15 | Total v... |
| Pvap | 0.37 | kPa | 288.15 | Total v... |
| Pvap | 0.37 | kPa | 288.15 | Total v... |
| Pvap | 0.37 | kPa | 288.15 | Isother... |
| Pvap | 0.52 | kPa | 293.15 | Total v... |
| Pvap | 0.52 | kPa | 293.15 | Isother... |
| Pvap | 0.52 | kPa | 293.15 | Total v... |
| Pvap | 0.71 | kPa | 298.15 | Total v... |
| Pvap | 0.71 | kPa | 298.15 | Total v... |
| Pvap | 0.71 | kPa | 298.15 | Isother... |
| Pvap | 0.98 | kPa | 303.15 | Isother... |
| Pvap | 0.98 | kPa | 303.15 | Total v... |
| Pvap | 0.98 | kPa | 303.15 | Total v... |
| Pvap | 1.29 | kPa | 308.15 | Isother... |
| Pvap | 1.29 | kPa | 308.15 | Total v... |
| Pvap | 1.29 | kPa | 308.15 | Total v... |
| Pvap | 1.70 | kPa | 313.15 | Total v... |
| Pvap | 1.70 | kPa | 313.15 | Isother... |
| Pvap | 1.70 | kPa | 313.15 | Total v... |
| Pvap | 2.24 | kPa | 318.15 | Total v... |
| Pvap | 2.24 | kPa | 318.15 | Total v... |
| Pvap | 2.24 | kPa | 318.15 | Isother... |
| Pvap | 2.86 | kPa | 323.15 | Total v... |
| Pvap | 2.86 | kPa | 323.15 | Total v... |
| Pvap | 2.86 | kPa | 323.15 | Isother... |
| Pvap | 95.50 | kPa | 417.25 | Vapor-l... |
| n0 | [1.48650; 1.49400] | [293.15; 308.15] |
|
|
|
T(K) Refractive Index 1.49 1.49 1.49 1.49 1.49 295 300 305 | ||||
| n0 | 1.49400 | 293.15 | Activit... | |
| n0 | 1.49400 | 293.15 | Excess ... | |
| n0 | 1.49387 | 293.15 | Densiti... | |
| n0 | 1.49400 | 293.15 | Bubble ... | |
| n0 | 1.49400 | 293.15 | Bubble ... | |
| n0 | 1.49400 | 293.15 | Vapor-L... | |
| n0 | 1.49200 | 298.15 | Isother... | |
| n0 | 1.49140 | 298.15 | Bubble ... | |
| n0 | 1.49400 | 298.15 | Bubble ... | |
| n0 | 1.49140 | 298.15 | Bubble-... | |
| n0 | 1.49220 | 298.15 | Density... | |
| n0 | 1.48887 | 303.15 | Densiti... | |
| n0 | 1.48940 | 303.15 | Density... | |
| n0 | 1.48810 | 303.15 | Densiti... | |
| n0 | 1.48650 | 308.15 | Density... | |
| ρl | [1556.07; 1604.78] | kg/m3 | [288.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 1560 1570 1580 1590 1600 290 300 310 | ||||
| ρl | 1601.45 | kg/m3 | 288.15 | Volumet... |
| ρl | 1602.77 | kg/m3 | 288.15 | Densiti... |
| ρl | 1604.78 | kg/m3 | 288.15 | Densiti... |
| ρl | 1604.75 | kg/m3 | 288.15 | Densiti... |
| ρl | 1600.00 | kg/m3 | 293.00 | KDB |
| ρl | 1593.65 | kg/m3 | 293.15 | Volumet... |
| ρl | 1594.57 | kg/m3 | 293.20 | Isobari... |
| ρl | 1589.19 | kg/m3 | 298.15 | Densiti... |
| ρl | 1586.80 | kg/m3 | 298.15 | Excess ... |
| ρl | 1585.87 | kg/m3 | 298.15 | Volumet... |
| ρl | 1587.60 | kg/m3 | 298.15 | Volumet... |
| ρl | 1587.20 | kg/m3 | 298.15 | Densiti... |
| ρl | 1589.18 | kg/m3 | 298.15 | Densiti... |
| ρl | 1586.22 | kg/m3 | 298.15 | Thermod... |
| ρl | 1588.23 | kg/m3 | 298.15 | Volumet... |
| ρl | 1579.60 | kg/m3 | 303.15 | Excess ... |
| ρl | 1578.07 | kg/m3 | 303.15 | Volumet... |
| ρl | 1573.59 | kg/m3 | 308.15 | Densiti... |
| ρl | 1571.63 | kg/m3 | 308.15 | Densiti... |
| ρl | 1573.57 | kg/m3 | 308.15 | Densiti... |
| ρl | 1570.27 | kg/m3 | 308.15 | Volumet... |
| ρl | 1570.60 | kg/m3 | 308.15 | Excess ... |
| ρl | 1572.66 | kg/m3 | 308.15 | Volumet... |
| ρl | 1562.45 | kg/m3 | 313.15 | Volumet... |
| ρl | 1563.70 | kg/m3 | 313.15 | Excess ... |
| ρl | 1557.94 | kg/m3 | 318.15 | Densiti... |
| ρl | 1556.07 | kg/m3 | 318.15 | Densiti... |
| ρl | 1557.04 | kg/m3 | 318.15 | Volumet... |
| ρl | 1557.95 | kg/m3 | 318.15 | Densiti... |
| ΔfusS | [1.74; 41.50] | J/mol×K | [204.80; 230.80] |
|
| ΔfusS | 1.74 | J/mol×K | 204.80 | NIST |
| ΔfusS | 2.62 | J/mol×K | 207.30 | NIST |
| ΔfusS | 41.50 | J/mol×K | 230.30 | NIST |
| ΔfusS | 39.74 | J/mol×K | 230.80 | NIST |
| csound,fluid | [1087.00; 1150.61] | m/s | [298.15; 318.15] |
|
| csound,fluid | 1150.61 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1118.66 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1087.00 | m/s | 318.15 | Speeds ... |
| γ | 0.03 | N/m | 293.20 | KDB |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 308.15 | 101.00 | 0.0013 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [309.36; 447.30] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.38082e+01 | |||
| Coefficient B | -3.15431e+03 | |||
| Coefficient C | -7.60640e+01 | |||
| Temperature range, min. | 309.36 | |||
| Temperature range, max. | 447.30 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 309.36 | Calculated Property |
| Pvap | 3.07 | kPa | 324.69 | Calculated Property |
| Pvap | 6.41 | kPa | 340.01 | Calculated Property |
| Pvap | 12.35 | kPa | 355.34 | Calculated Property |
| Pvap | 22.23 | kPa | 370.67 | Calculated Property |
| Pvap | 37.74 | kPa | 385.99 | Calculated Property |
| Pvap | 60.97 | kPa | 401.32 | Calculated Property |
| Pvap | 94.32 | kPa | 416.65 | Calculated Property |
| Pvap | 140.55 | kPa | 431.97 | Calculated Property |
| Pvap | 202.65 | kPa | 447.30 | Calculated Property |
| Pvap | [1.26e-03; 5791.60] | kPa | [229.35; 661.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.48935e+02 | |||
| Coefficient B | -1.09840e+04 | |||
| Coefficient C | -1.99490e+01 | |||
| Coefficient D | 1.34830e-05 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 661.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 600 | ||||
| Pvap | 1.26e-03 | kPa | 229.35 | Calculated Property |
| Pvap | 0.16 | kPa | 277.31 | Calculated Property |
| Pvap | 3.30 | kPa | 325.27 | Calculated Property |
| Pvap | 25.56 | kPa | 373.23 | Calculated Property |
| Pvap | 109.33 | kPa | 421.19 | Calculated Property |
| Pvap | 325.30 | kPa | 469.16 | Calculated Property |
| Pvap | 774.51 | kPa | 517.12 | Calculated Property |
| Pvap | 1612.42 | kPa | 565.08 | Calculated Property |
| Pvap | 3111.67 | kPa | 613.04 | Calculated Property |
| Pvap | 5791.60 | kPa | 661.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1,1,2,2-tetrachloro-.
Mixtures
- Benzene + Ethane, 1,1,2,2-tetrachloro-
- Carbon Tetrachloride + Ethane, 1,1,2,2-tetrachloro-
- Phenol, 2-methyl- + Ethane, 1,1,2,2-tetrachloro-
- Ethane, 1,2-dibromo- + Ethane, 1,1,2,2-tetrachloro-
- Formamide, N,N-dimethyl- + Ethane, 1,1,2,2-tetrachloro-
- Toluene + Ethane, 1,1,2,2-tetrachloro-
- Ethylbenzene + Ethane, 1,1,2,2-tetrachloro-
- Benzene, propyl- + Ethane, 1,1,2,2-tetrachloro-
- Benzene, (1-methylethyl)- + Ethane, 1,1,2,2-tetrachloro-
- Benzene, n-butyl- + Ethane, 1,1,2,2-tetrachloro-
- Benzene, (1-methylpropyl)- + Ethane, 1,1,2,2-tetrachloro-
- Benzene, tert-butyl- + Ethane, 1,1,2,2-tetrachloro-
- Heptane + Ethane, 1,1,2,2-tetrachloro-
- Cyclohexane + Ethane, 1,1,2,2-tetrachloro-
- 2-Propenenitrile + Ethane, 1,1,2,2-tetrachloro-
- Methane, nitro- + Ethane, 1,1,2,2-tetrachloro-
- Tetrahydrofuran + Ethane, 1,1,2,2-tetrachloro-
- 1-Pentanol + Ethane, 1,1,2,2-tetrachloro-
- 1-Hexanol + Ethane, 1,1,2,2-tetrachloro-
- 1-Octanol + Ethane, 1,1,2,2-tetrachloro-
Find more mixtures with Ethane, 1,1,2,2-tetrachloro-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
- Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
- 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
- Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
- Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
- 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
- Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
- Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
- Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
- Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
- Isothermal (vapour + liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15) K
- Densities and viscosities of binary liquid mixtures of N-methylacetamide with some chloroethanes and chloroethenes at T = 308.15 K
- Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
- Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
- Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
- Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
- Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
- Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
- Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
- Densities and Excess Molar Volumes of the Ternary System (1,4-Dioxane + 2-Propanol + 1,1,2,2-Tetrachloroethane) at T = 288.15-318.15 K and at Atmospheric Pressure: Experimental Measurements and Prigogine-Flory-Patterson Modeling
- Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
- Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
- 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
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) 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
- Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
- Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
- 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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