- InChI
- InChI=1S/C4H8O2/c1-2-6-4-3-5-1/h1-4H2
- InChI Key
- RYHBNJHYFVUHQT-UHFFFAOYSA-N
- Formula
- C4H8O2
- SMILES
- C1COCCO1
- Molecular Weight1
- 88.11
- CAS
- 123-91-1
- Other Names
-
- 1,4-Diethylene dioxide
- 1,4-Diethyleneoxide
- 1,4-Dioxacyclohexane
- 1,4-Dioxan
- 1,4-Dioxin, tetrahydro-
- DIETHYLENE DIOXIDE
- DIETHYLENE ETHER
- Di(ethylene oxide)
- Diokan
- Dioksan
- Diossano-1,4
- Dioxaan-1,4
- Dioxan
- Dioxan-1,4
- Dioxane
- Dioxane-1,4
- Dioxanne
- Dioxyethylene ether
- Glycol ethylene ether
- Glycol ethylene ether 8
- NCI-C03689
- NE 220
- NSC 8728
- P-DIOXANE
- Rcra waste number U108
- Tetrahydro-1,4-dioxin
- Tetrahydro-p-dioxin
- UN 1165
- p-Dioxan
- p-Dioxin, tetrahydro-
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- 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).
- σcond : Electrical conductivity (S/m).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- 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).
- ΔsubH : Enthalpy of sublimation 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).
- ν : Kinematic viscosity (m2/s).
- 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.
- D*i : Self diffusion coefficient (m2/s).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (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).
- Tfus : Melting 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 | 0.2810 | KDB | |
| PAff | 797.40 | kJ/mol | NIST |
| Tig | 453.15 | K | KDB |
| BasG | 770.00 | kJ/mol | NIST |
| ΔcH°liquid | [-2363.90; -2186.80] | kJ/mol |
|
| ΔcH°liquid | -2362.23 ± 0.99 | kJ/mol | NIST |
| ΔcH°liquid | -2363.90 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | -2346.20 | kJ/mol | NIST |
| ΔcH°liquid | -2186.80 | kJ/mol | NIST |
| μ | 0.40 | debye | KDB |
| η | 0.0011960 | Pa×s | Excess ... |
| LFL | 1.97 | % in Air | KDB |
| UFL | 22.50 | % in Air | KDB |
| Tflash,cc | 296.48 | K | KDB |
| Tflash,oc | 285.37 | K | KDB |
| ΔfG° | -180.90 | kJ/mol | KDB |
| Rg | 3.1100 | KDB | |
| ΔfH°gas | [-318.00; -315.30] | kJ/mol |
|
| ΔfH°gas | -315.30 | kJ/mol | KDB |
| ΔfH°gas | -315.30 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -318.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | [-355.13; -353.50] | kJ/mol |
|
| ΔfH°liquid | -355.13 ± 0.86 | kJ/mol | NIST |
| ΔfH°liquid | -353.50 ± 0.80 | kJ/mol | NIST |
| ΔfusH° | 12.84 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 34.26 | kJ/mol | Joback Calculated Property |
| IE | [9.13; 9.43] | eV |
|
| IE | 9.19 ± 0.01 | eV | NIST |
| IE | 9.19 ± 0.01 | eV | NIST |
| IE | 9.13 ± 0.03 | eV | NIST |
| IE | 9.40 | eV | NIST |
| IE | 9.43 | eV | NIST |
| IE | 9.41 | eV | NIST |
| IE | 9.30 ± 0.10 | eV | NIST |
| IE | 9.43 | eV | NIST |
| log10WS | 0.43 | Crippen Calculated Property | |
| logPoct/wat | 0.033 | Crippen Calculated Property | |
| McVol | 68.100 | ml/mol | McGowan Calculated Property |
| Pc | [5000.00; 5471.55] | kPa |
|
| Pc | 5210.00 | kPa | KDB |
| Pc | 5471.55 ± 303.98 | kPa | NIST |
| Pc | 5210.00 ± 68.94 | kPa | NIST |
| Pc | 5000.00 ± 70.00 | kPa | NIST |
| ρc | 360.35 ± 9.69 | kg/m3 | NIST |
| Inp | [643.00; 731.30] |
|
|
| Inp | 670.10 | NIST | |
| Inp | Outlier 648.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 669.70 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | Outlier 731.30 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | Outlier 643.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | Outlier 648.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 702.00 | NIST | |
| Inp | 660.30 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | Outlier 651.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 702.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 687.00 | NIST | |
| I | [1065.00; 1105.00] |
|
|
| I | 1065.00 | NIST | |
| I | 1093.00 | NIST | |
| I | 1097.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1066.00 | NIST | |
| I | 1085.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1083.00 | NIST | |
| I | 1083.00 | NIST | |
| I | 1068.00 | NIST | |
| I | 1084.00 | NIST | |
| I | 1066.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1083.00 | NIST | |
| S°gas | 299.91 | J/mol×K | NIST |
| S°liquid | 196.60 | J/mol×K | NIST |
| Tboil | [374.45; 374.60] | K |
|
| Tboil | 374.60 | K | KDB |
| Tboil | 374.45 | K | Measure... |
| Tboil | 374.47 | K | Study o... |
| Tboil | 374.52 | K | Vapor-L... |
| Tc | [585.15; 588.15] | K |
|
| Tc | 587.00 | K | KDB |
| Tc | 587.30 ± 1.00 | K | NIST |
| Tc | 588.15 ± 2.00 | K | NIST |
| Tc | 588.00 ± 2.00 | K | NIST |
| Tc | 585.15 ± 2.00 | K | NIST |
| Tfus | [284.48; 284.90] | K |
|
| Tfus | 284.90 | K | KDB |
| Tfus | 284.48 | K | Efficie... |
| Ttriple | 284.10 ± 0.20 | K | NIST |
| Vc | [0.238; 0.239] | m3/kmol |
|
| Vc | 0.238 | m3/kmol | KDB |
| Vc | 0.239 ± 0.008 | m3/kmol | NIST |
| Vc | 0.239 ± 0.004 | m3/kmol | NIST |
| Zc | 0.2540620 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [118.28; 176.66] | J/mol×K | [369.04; 578.47] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 120 130 140 150 160 170 180 400 450 500 550 | ||||
| Cp,gas | 118.28 | J/mol×K | 369.04 | Joback Calculated Property |
| Cp,gas | 129.39 | J/mol×K | 403.94 | Joback Calculated Property |
| Cp,gas | 139.92 | J/mol×K | 438.85 | Joback Calculated Property |
| Cp,gas | 149.90 | J/mol×K | 473.75 | Joback Calculated Property |
| Cp,gas | 159.34 | J/mol×K | 508.66 | Joback Calculated Property |
| Cp,gas | 168.26 | J/mol×K | 543.56 | Joback Calculated Property |
| Cp,gas | 176.66 | J/mol×K | 578.47 | Joback Calculated Property |
| Cp,liquid | [140.20; 160.40] | J/mol×K | [288.15; 333.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 140 145 150 155 160 300 320 | ||||
| Cp,liquid | 146.70 | J/mol×K | 288.15 | Thermop... |
| Cp,liquid | 146.00 | J/mol×K | 291.00 | NIST |
| Cp,liquid | 150.00 | J/mol×K | 293.15 | Thermop... |
| Cp,liquid | 154.80 | J/mol×K | 296.00 | NIST |
| Cp,liquid | 149.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 147.90 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 155.60 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 140.20 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 151.00 | J/mol×K | 298.15 | Thermop... |
| Cp,liquid | 147.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 149.65 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 150.57 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 149.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 150.65 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 150.77 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 149.73 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 149.49 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 152.97 | J/mol×K | 298.20 | NIST |
| Cp,liquid | 152.10 | J/mol×K | 303.15 | Thermop... |
| Cp,liquid | 153.70 | J/mol×K | 308.15 | Thermop... |
| Cp,liquid | 155.30 | J/mol×K | 313.15 | Thermop... |
| Cp,liquid | 156.50 | J/mol×K | 318.15 | Thermop... |
| Cp,liquid | 158.40 | J/mol×K | 323.15 | Thermop... |
| Cp,liquid | 160.20 | J/mol×K | 328.15 | Thermop... |
| Cp,liquid | 160.40 | J/mol×K | 333.15 | Thermop... |
| η | [0.0005770; 0.0015900] | Pa×s | [283.15; 353.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 300 320 340 | ||||
| η | 0.0015900 | Pa×s | 283.15 | Densiti... |
| η | 0.0014400 | Pa×s | 288.15 | Viscosi... |
| η | 0.0014381 | Pa×s | 288.15 | Densiti... |
| η | 0.0012860 | Pa×s | 293.15 | Viscosi... |
| η | 0.0013111 | Pa×s | 293.15 | Densiti... |
| η | 0.0013120 | Pa×s | 293.15 | Densiti... |
| η | 0.0011780 | Pa×s | 298.15 | Studies... |
| η | 0.0012023 | Pa×s | 298.15 | Densiti... |
| η | 0.0011850 | Pa×s | 298.15 | Viscosi... |
| η | 0.0011800 | Pa×s | 298.15 | Viscosi... |
| η | 0.0012236 | Pa×s | 298.15 | Densiti... |
| η | 0.0011020 | Pa×s | 303.15 | Densiti... |
| η | 0.0010870 | Pa×s | 303.15 | Viscosi... |
| η | 0.0011065 | Pa×s | 303.15 | Densiti... |
| η | 0.0010983 | Pa×s | 303.15 | Viscosi... |
| η | 0.0010985 | Pa×s | 303.15 | Viscosi... |
| η | 0.0009985 | Pa×s | 308.15 | Studies... |
| η | 0.0010290 | Pa×s | 308.15 | Viscosi... |
| η | 0.0010219 | Pa×s | 308.15 | Densiti... |
| η | 0.0010295 | Pa×s | 308.15 | Viscosi... |
| η | 0.0009268 | Pa×s | 308.15 | Densiti... |
| η | 0.0009575 | Pa×s | 313.15 | Viscosi... |
| η | 0.0009477 | Pa×s | 313.15 | Densiti... |
| η | 0.0009460 | Pa×s | 313.15 | Densiti... |
| η | 0.0009340 | Pa×s | 313.15 | Viscosi... |
| η | 0.0007991 | Pa×s | 318.15 | Densiti... |
| η | 0.0008909 | Pa×s | 318.15 | Studies... |
| η | 0.0008140 | Pa×s | 323.15 | Viscosi... |
| η | 0.0008250 | Pa×s | 323.15 | Densiti... |
| η | 0.0007180 | Pa×s | 333.15 | Viscosi... |
| η | 0.0007210 | Pa×s | 333.15 | Densiti... |
| η | 0.0006400 | Pa×s | 343.15 | Densiti... |
| η | 0.0006400 | Pa×s | 343.15 | Viscosi... |
| η | 0.0005770 | Pa×s | 353.15 | Viscosi... |
| σcond | [0.00; 0.00] | S/m | [298.15; 323.15] |
|
| σcond | 0.00 | S/m | 298.15 | Micella... |
| σcond | 0.00 | S/m | 303.15 | Micella... |
| σcond | 0.00 | S/m | 315.15 | Micella... |
| σcond | 0.00 | S/m | 323.15 | Micella... |
| ΔfusH | [2.35; 12.84] | kJ/mol | [272.90; 284.10] |
|
| ΔfusH | 2.35 | kJ/mol | 272.90 | NIST |
| ΔfusH | 11.88 | kJ/mol | 283.20 | NIST |
| ΔfusH | 12.84 | kJ/mol | 284.10 | NIST |
| ΔfusH | 12.84 | kJ/mol | 284.10 | NIST |
| ΔsubH | 35.60 | kJ/mol | 254.50 | NIST |
| ΔvapH | [34.16; 38.00] | kJ/mol | [273.00; 374.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 35 36 37 38 300 350 | ||||
| ΔvapH | 35.80 | kJ/mol | 273.00 | NIST |
| ΔvapH | 37.00 | kJ/mol | 318.00 | NIST |
| ΔvapH | 38.00 | kJ/mol | 330.00 | NIST |
| ΔvapH | 37.30 | kJ/mol | 345.50 | NIST |
| ΔvapH | 36.50 | kJ/mol | 350.50 | NIST |
| ΔvapH | 34.16 | kJ/mol | 374.50 | NIST |
| ν | [0.0000009; 0.0000011] | m2/s | [298.15; 313.15] |
|
| ν | 0.0000011 | m2/s | 298.15 | Experim... |
| ν | 0.0000009 | m2/s | 313.15 | Experim... |
| Pvap | [2.38; 19.54] | kPa | [285.11; 328.15] |
|
|
T(K) Vapor pressure (kPa) 5 10 15 20 290 300 310 320 | ||||
| Pvap | 2.38 | kPa | 285.11 | Vapor P... |
| Pvap | 2.70 | kPa | 288.15 | Vapor P... |
| Pvap | 2.92 | kPa | 288.66 | Vapor P... |
| Pvap | 3.60 | kPa | 292.45 | Vapor P... |
| Pvap | 4.50 | kPa | 296.56 | Vapor P... |
| Pvap | 4.50 | kPa | 296.57 | Vapor P... |
| Pvap | 4.90 | kPa | 298.15 | Isother... |
| Pvap | 4.90 | kPa | 298.15 | Isother... |
| Pvap | 4.97 | kPa | 298.15 | Vapor P... |
| Pvap | 5.34 | kPa | 299.81 | Vapor P... |
| Pvap | 6.21 | kPa | 302.92 | Vapor P... |
| Pvap | 7.58 | kPa | 306.93 | Vapor P... |
| Pvap | 7.57 | kPa | 306.94 | Vapor P... |
| Pvap | 8.12 | kPa | 308.15 | Vapor P... |
| Pvap | 9.19 | kPa | 311.04 | Vapor P... |
| Pvap | 10.17 | kPa | 313.15 | Isother... |
| Pvap | 10.31 | kPa | 313.38 | Vapor P... |
| Pvap | 10.29 | kPa | 313.38 | Vapor P... |
| Pvap | 19.54 | kPa | 328.15 | Isother... |
| Pvap | 19.54 | kPa | 328.15 | Isother... |
| n0 | [1.40840; 1.42450] | [288.15; 318.20] |
|
|
|
T(K) Refractive Index 1.41 1.42 1.42 1.43 290 300 310 | ||||
| n0 | 1.42450 | 288.15 | Densiti... | |
| n0 | 1.42200 | 293.10 | Liquid ... | |
| n0 | 1.42200 | 293.10 | Liquid-... | |
| n0 | 1.42240 | 293.15 | Densiti... | |
| n0 | 1.41750 | 293.15 | Solubil... | |
| n0 | 1.42020 | 298.15 | Density... | |
| n0 | 1.42030 | 298.15 | Densiti... | |
| n0 | 1.41995 | 298.15 | Volumet... | |
| n0 | 1.42030 | 298.15 | Bubble ... | |
| n0 | 1.42010 | 298.15 | Density... | |
| n0 | 1.41810 | 298.15 | Density... | |
| n0 | 1.42030 | 298.15 | Density... | |
| n0 | 1.42010 | 298.15 | Density... | |
| n0 | 1.42000 | 298.20 | A therm... | |
| n0 | 1.41700 | 303.15 | Density... | |
| n0 | 1.41820 | 303.15 | Densiti... | |
| n0 | 1.41700 | 303.15 | Density... | |
| n0 | 1.41760 | 303.15 | Density... | |
| n0 | 1.41640 | 303.15 | Density... | |
| n0 | 1.41810 | 303.15 | Thermod... | |
| n0 | 1.41450 | 308.15 | Density... | |
| n0 | 1.41430 | 308.15 | Density... | |
| n0 | 1.41410 | 308.15 | Density... | |
| n0 | 1.41440 | 308.15 | Density... | |
| n0 | 1.41610 | 308.15 | Densiti... | |
| n0 | 1.41430 | 308.20 | A therm... | |
| n0 | 1.41440 | 308.20 | A therm... | |
| n0 | 1.41264 | 313.15 | Volumet... | |
| n0 | 1.41390 | 313.15 | Densiti... | |
| n0 | 1.41170 | 318.15 | Densiti... | |
| n0 | 1.40920 | 318.20 | A therm... | |
| n0 | 1.40840 | 318.20 | A therm... | |
| ρl | [964.63; 1039.12] | kg/m3 | [288.15; 353.15] |
|
|
T(K) Liquid Density (kg/m3) 960 980 1000 1020 1040 300 320 340 | ||||
| ρl | 1039.12 | kg/m3 | 288.15 | Densiti... |
| ρl | 1038.78 | kg/m3 | 288.15 | Volumet... |
| ρl | 1033.00 | kg/m3 | 293.00 | KDB |
| ρl | 1033.57 | kg/m3 | 293.15 | Density... |
| ρl | 1033.50 | kg/m3 | 293.15 | Experim... |
| ρl | 1033.16 | kg/m3 | 293.15 | Volumet... |
| ρl | 1033.80 | kg/m3 | 293.15 | Volumet... |
| ρl | 1033.59 | kg/m3 | 293.15 | Thermod... |
| ρl | 1027.88 | kg/m3 | 298.15 | (Vapour... |
| ρl | 1027.87 | kg/m3 | 298.15 | Surface... |
| ρl | 1027.90 | kg/m3 | 298.15 | Densiti... |
| ρl | 1027.84 | kg/m3 | 298.15 | Densiti... |
| ρl | 1027.79 | kg/m3 | 298.15 | Hydroge... |
| ρl | 1027.51 | kg/m3 | 298.15 | Volumet... |
| ρl | 1027.90 | kg/m3 | 298.15 | Vapour ... |
| ρl | 1027.85 | kg/m3 | 298.15 | Experim... |
| ρl | 1027.85 | kg/m3 | 298.15 | Experim... |
| ρl | 1027.82 | kg/m3 | 298.15 | Surface... |
| ρl | 1027.94 | kg/m3 | 298.15 | Thermod... |
| ρl | 1027.92 | kg/m3 | 298.15 | Density... |
| ρl | 1027.87 | kg/m3 | 298.15 | Isother... |
| ρl | 1027.99 | kg/m3 | 298.15 | Densiti... |
| ρl | 1028.20 | kg/m3 | 298.15 | Densiti... |
| ρl | 1022.30 | kg/m3 | 303.15 | Studies... |
| ρl | 1022.27 | kg/m3 | 303.15 | Density... |
| ρl | 1022.19 | kg/m3 | 303.15 | Experim... |
| ρl | 1021.84 | kg/m3 | 303.15 | Volumet... |
| ρl | 1022.40 | kg/m3 | 303.15 | Unravel... |
| ρl | 1022.30 | kg/m3 | 303.15 | Densiti... |
| ρl | 1022.70 | kg/m3 | 303.15 | Densiti... |
| ρl | 1022.28 | kg/m3 | 303.15 | Thermod... |
| ρl | 1022.33 | kg/m3 | 303.15 | Densiti... |
| ρl | 1016.57 | kg/m3 | 308.15 | Densiti... |
| ρl | 1016.66 | kg/m3 | 308.15 | Densiti... |
| ρl | 1016.59 | kg/m3 | 308.15 | Thermod... |
| ρl | 1016.78 | kg/m3 | 308.15 | Hydroge... |
| ρl | 1016.60 | kg/m3 | 308.15 | Densiti... |
| ρl | 1017.40 | kg/m3 | 308.15 | Densiti... |
| ρl | 1016.52 | kg/m3 | 308.15 | Experim... |
| ρl | 1010.98 | kg/m3 | 313.15 | Densiti... |
| ρl | 1011.10 | kg/m3 | 313.15 | Densiti... |
| ρl | 1010.83 | kg/m3 | 313.15 | Experim... |
| ρl | 1010.91 | kg/m3 | 313.15 | Density... |
| ρl | 1005.29 | kg/m3 | 318.15 | Densiti... |
| ρl | 1005.28 | kg/m3 | 318.15 | Densiti... |
| ρl | 1005.24 | kg/m3 | 318.15 | Hydroge... |
| ρl | 1005.12 | kg/m3 | 318.15 | Experim... |
| ρl | 999.49 | kg/m3 | 323.15 | Density... |
| ρl | 999.58 | kg/m3 | 323.15 | Densiti... |
| ρl | 999.40 | kg/m3 | 323.15 | Experim... |
| ρl | 987.97 | kg/m3 | 333.15 | Density... |
| ρl | 976.37 | kg/m3 | 343.15 | Density... |
| ρl | 964.63 | kg/m3 | 353.15 | Density... |
| D*i | [0.00; 0.00] | m2/s | [288.31; 358.49] |
|
|
T(K) Self diffusion coefficient (m2/s) 1.00e-9 1.50e-9 2.00e-9 2.50e-9 300 320 340 360 | ||||
| D*i | 0.00 | m2/s | 288.31 | Viscous... |
| D*i | 0.00 | m2/s | 288.33 | Viscous... |
| D*i | 0.00 | m2/s | 293.11 | Viscous... |
| D*i | 0.00 | m2/s | 298.13 | Viscous... |
| D*i | 0.00 | m2/s | 298.17 | Viscous... |
| D*i | 0.00 | m2/s | 298.18 | Viscous... |
| D*i | 0.00 | m2/s | 298.20 | Viscous... |
| D*i | 0.00 | m2/s | 303.12 | Viscous... |
| D*i | 0.00 | m2/s | 307.92 | Viscous... |
| D*i | 0.00 | m2/s | 308.06 | Viscous... |
| D*i | 0.00 | m2/s | 317.85 | Viscous... |
| D*i | 0.00 | m2/s | 318.24 | Viscous... |
| D*i | 0.00 | m2/s | 327.94 | Viscous... |
| D*i | 0.00 | m2/s | 327.95 | Viscous... |
| D*i | 0.00 | m2/s | 338.09 | Viscous... |
| D*i | 0.00 | m2/s | 338.12 | Viscous... |
| D*i | 0.00 | m2/s | 338.13 | Viscous... |
| D*i | 0.00 | m2/s | 347.87 | Viscous... |
| D*i | 0.00 | m2/s | 347.97 | Viscous... |
| D*i | 0.00 | m2/s | 358.25 | Viscous... |
| D*i | 0.00 | m2/s | 358.49 | Viscous... |
| ΔfusS | [8.79; 45.19] | J/mol×K | [272.90; 284.10] |
|
| ΔfusS | 8.79 | J/mol×K | 272.90 | NIST |
| ΔfusS | 41.90 | J/mol×K | 283.20 | NIST |
| ΔfusS | 45.19 | J/mol×K | 284.10 | NIST |
| csound,fluid | [1258.60; 1409.60] | m/s | [283.15; 318.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1250 1300 1350 1400 290 300 310 | ||||
| csound,fluid | 1409.60 | m/s | 283.15 | Speeds ... |
| csound,fluid | 1367.20 | m/s | 293.15 | Physico... |
| csound,fluid | 1357.70 | m/s | 295.15 | Density... |
| csound,fluid | 1343.60 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1344.80 | m/s | 298.15 | Densiti... |
| csound,fluid | 1346.30 | m/s | 298.15 | Compres... |
| csound,fluid | 1344.70 | m/s | 298.15 | Physico... |
| csound,fluid | 1344.80 | m/s | 298.15 | Density... |
| csound,fluid | 1331.90 | m/s | 301.15 | Density... |
| csound,fluid | 1323.10 | m/s | 303.15 | Physico... |
| csound,fluid | 1319.00 | m/s | 304.15 | Density... |
| csound,fluid | 1306.20 | m/s | 307.15 | Density... |
| csound,fluid | 1301.20 | m/s | 308.15 | Physico... |
| csound,fluid | 1293.30 | m/s | 310.15 | Density... |
| csound,fluid | 1279.70 | m/s | 313.15 | Physico... |
| csound,fluid | 1279.80 | m/s | 313.15 | Densiti... |
| csound,fluid | 1278.80 | m/s | 313.15 | Speeds ... |
| csound,fluid | 1280.40 | m/s | 313.15 | Density... |
| csound,fluid | 1258.60 | m/s | 318.15 | Physico... |
| γ | [0.03; 0.04] | N/m | [283.15; 313.15] |
|
| γ | 0.04 | N/m | 283.15 | Thermop... |
| γ | 0.03 | N/m | 298.15 | Thermop... |
| γ | 0.03 | N/m | 313.15 | Thermop... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tfus | 285.08 | K | 101.30 | (Solid ... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0011 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0010 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 85.90 | 298.15 | 1027.93 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [274.07; 398.83] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48111e+01 | |||
| Coefficient B | -3.42606e+03 | |||
| Coefficient C | -3.81740e+01 | |||
| Temperature range, min. | 274.07 | |||
| Temperature range, max. | 398.83 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 274.07 | Calculated Property |
| Pvap | 2.99 | kPa | 287.93 | Calculated Property |
| Pvap | 6.14 | kPa | 301.79 | Calculated Property |
| Pvap | 11.75 | kPa | 315.66 | Calculated Property |
| Pvap | 21.15 | kPa | 329.52 | Calculated Property |
| Pvap | 36.08 | kPa | 343.38 | Calculated Property |
| Pvap | 58.76 | kPa | 357.24 | Calculated Property |
| Pvap | 91.88 | kPa | 371.11 | Calculated Property |
| Pvap | 138.64 | kPa | 384.97 | Calculated Property |
| Pvap | 202.67 | kPa | 398.83 | Calculated Property |
| Pvap | [1.26; 5195.37] | kPa | [275.00; 587.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.69176e+01 | |||
| Coefficient B | -7.07594e+03 | |||
| Coefficient C | -9.15152e+00 | |||
| Coefficient D | 5.90158e-06 | |||
| Temperature range, min. | 275.00 | |||
| Temperature range, max. | 587.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
| Pvap | 1.26 | kPa | 275.00 | Calculated Property |
| Pvap | 8.54 | kPa | 309.67 | Calculated Property |
| Pvap | 36.89 | kPa | 344.33 | Calculated Property |
| Pvap | 116.49 | kPa | 379.00 | Calculated Property |
| Pvap | 294.01 | kPa | 413.67 | Calculated Property |
| Pvap | 630.26 | kPa | 448.33 | Calculated Property |
| Pvap | 1197.33 | kPa | 483.00 | Calculated Property |
| Pvap | 2078.30 | kPa | 517.67 | Calculated Property |
| Pvap | 3370.87 | kPa | 552.33 | Calculated Property |
| Pvap | 5195.37 | kPa | 587.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,4-Dioxane.
Mixtures
- Cyclopentane + 1,4-Dioxane
- 1,4-Dioxane + Cyclohexane
- Benzene + 1,4-Dioxane
- Propylene Carbonate + 1,4-Dioxane
- 2-Pyrrolidinone, 1-methyl- + 1,4-Dioxane
- Pentane, 1-chloro- + 1,4-Dioxane
- Hexane, 1-chloro- + 1,4-Dioxane
- 1-Propanol, 2-methyl- + 1,4-Dioxane
- 2-Propanol, 2-methyl- + 1,4-Dioxane
- 1-Butanol + 1,4-Dioxane
- n-Propyl chloride + 1,4-Dioxane
- 1,4-Dioxane + Water + 1,6-Octadiene, 3,7-dimethyl-
- 1,4-Dioxane + Ethylenediamine
- Ethane, 1,2-dichloro- + 1,4-Dioxane
- Monoethanolamine + 1,4-Dioxane
- n-Hexane + 1,4-Dioxane + Benzylamine
- Toluene + Pyrazinamide + 1,4-Dioxane
- Pyrazinamide + 1,4-Dioxane + Cyclohexane
- 1,4-Dioxane + Water
- Butane, 1-chloro- + 1,4-Dioxane
Find more mixtures with 1,4-Dioxane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
- Viscosity Behavior of Some Oxygen Containing Compounds
- (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
- Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
- Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
- Experimental and predicted excess molar enthalpies for 1,4-dioxane + octane + cyclohexane at 303.15 K
- Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
- Liquid liquid equilibria and partitioning in organic aqueous systems
- Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
- Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
- Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
- Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
- Liquid liquid phase equilibria of the ternary system of water/1,4-dioxane/dihydromyrcene
- Density and refractive index measurements of critical mixture 1,4-dioxane + water + saturated KCl in homogenous phase region
- Solubility and preferential solvation of indomethacin in 1,4-dioxane + water solvent mixtures
- Solubility of citric, malonic, and malic acids in different solvents from 303.2 to 333.2 K
- Liquid-liquid equilibrium for the system water + 1,4-dioxane + cyclohexanol over the temperature range of 313.2 - 343.2 K
- Solid-liquid equilibrium (SLE) of ternary system 3-nitrophthalic acid + 4-nitrophthalic acid + 1,4-dioxane at (283.15, 293.15, 303.15, 313.15 and 323.15) K
- Effect of solvent on the volumetric behavior ofN,N' -salicylidenephenyl diamine (Salophen) Schiff base at differenttemperatures (288.15 - 318.15) K
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Solubility temperature dependence and preferential solvation of sulfadiazine in 1,4-dioxane + water co-solvent mixtures
- 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
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Measurement of the solubility of the salt of 2- mercaptobenzothiazole with cyclohexylamine and tert-butylamine in various solvents at low temperatures: Models and thermodynamic parameters
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Solubility of 1,1-diamino-2,2-dinitroethylene in different pure solvents and binary mixtures (dimethyl sulfoxide p water) and (N,N-dimethylformamide p water) at different temperatures
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Unravelling various types of non-covalent interactions of benzyl amine with ethers in n-hexane at 303.15 K by ultrasonic and DFT methods
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
- (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
- Excess molar enthalpies of ternary mixtures of (methanol, ethanol + 2-propanol + 1,4-dioxane) at T ? 298:15 K
- Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
- Volumetric properties of binary mixtures of (water + organic solvents) at temperatures between T = 288.15 K and T = 303.15 K at p = 0.1 MPa
- Thermophysical study of 1,4-dioxane with cycloalkane mixtures
- Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
- Isothermal compressibility and internal pressure studies of some non-electrolytes in aqueous solutions at low temperatures
- Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- Apparent molar volumes and apparent molar heat capacities of aqueous tetrahydrofuran, dimethyl sulfoxide, 1,4-dioxane, and 1,2-dimethoxyethane at temperatures from 278.15 K to 393.15 K and at the pressure 0.35 MPa
- Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
- Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
- Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
- Partial molar volumes of organic solutes in water. XXII. Cyclic ethers at temperatures (298 to 573) K and pressures up to 30 MPa
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Solubility and phase separation of 4-morpholinepropanesulfonic acid (MOPS), and 3-morpholino-2-hydroxypropanesulfonic acid (MOPSO) in aqueous 1,4-dioxane and ethanol solutions
- Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Aggregation properties and thermodynamics of micellization of gemini surfactants with diethyl ether spacer in water and water organic solvent mixed media
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Experimental and theoretical excess molar properties of imidazolium based ionic liquids with molecular organic solvents I. 1-Hexyl-3- methylimidazlouim tetraflouroborate and 1-octyl-3-methylimidazlouim tetraflouroborate with cyclic ethers
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Solubility of 3-chloro-N-phenylphthalimide in ten organic solvents from T = (288.15 to 323.15) K: Determination and modelling
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamic models for determination of the solubility of 4-(4-aminophenyl)-3-morpholinone in different pure solvents and (1,4-dioxane + ethyl acetate) binary mixtures with temperatures from (278.15 to 333.15) K
- Thermodynamic models for determination of 3-chloro-N-phenylphthalimide solubility in binary solvent mixtures of (acetone, ethyl acetate or 1,4-dioxane + methanol)
- Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
- Solid-liquid equilibrium and phase diagram for the ternary (2-naphthaldehyde + o-phthalic anhydride + 1,4-dioxane) system
- Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Thermodynamic study of the solubility of 2,4'-dihydroxydiphenyl sulfone in nine organic solvents from T = (278.15 to 313.15) K and thermodynamic properties of dissolution
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- 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
- Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
- Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
- Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
- Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
- Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
- Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
- Solubility of 3-methyl-4-nitrobenzoic acid in binary solvent mixtures of {(1,4-dioxane, N-methyl-2-pyrrolidone, N,N-dimethylformamide) + methanol} from T = (283.15 to 318.15) K: Experimental determination and thermodynamic modelling
- Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
- Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
- Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
- Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
- Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Solubility and preferential solvation of econazole nitrate in binary solvent mixtures of methanol, ethanol and 1,4-dioxane in water
- Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
- Solubility modelling and preferential solvation of paclobutrazol in cosolvent mixtures of (ethanol, n-propanol and 1,4-dioxane) + water
- Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Thermodynamic modelling of solubility and preferential solvation for ribavirin (II) in co-solvent mixtures of (methanol, n-propanol, acetonitrile or 1,4-dioxane) + water
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Equilibrium solubility and preferential solvation of 1,1'-sulfonylbis(4-aminobenzene) in binary aqueous solutions of n-propanol, isopropanol and 1,4-dioxane
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Excess molar volumes and excess isentropic compressibilities of mixtures containing lactam, cyclic ethers and cyclic alkanones
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Equilibrium solubility, solvent effect and preferential solvation of chlorhexidine in aqueous co-solvent solutions of (methanol, ethanol, N,N-dimethylformamide and 1,4-dioxane)
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
- Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
- Equilibrium solubility determination, modelling and thermodynamic aspects of 6-chloroguanine in aqueous co-solvent mixtures of N,N-dimethylformamide, isopropanol, 1,4-dioxane and dimethyl sulfoxide
- Solubility and preferential solvation of flubendazole dissolved in aqueous co-solvent mixtures of 1,4-dioxane, dimethyl sulfoxide, N,N-dimethylformamide and isopropanol
- Vapour-liquid phase boundaries including the near critical regions of the (CO2 + styrene, CO2 + 1,4-dioxane, and CO2 + N,N-dimethylformamide) systems
- The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
- Solubility modelling and thermodynamic aspect of d-aspartic acid in aqueous co-solvent mixtures of N-methyl-2-pyrrolidone, N,N-dimethylformamide, dimethyl sulfoxide and 1.4-dioxane
- Solubility of chloroxine in aqueous co-solvent mixtures of N,N-dimethylformamide, dimethyl sulfoxide, N-methyl-2-pyrrolidone and 1,4-dioxane: Determination, solvent effect and preferential solvation analysis
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Ternary excess molar enthalpies of (1-propanol + 2-propanol + 1,4-dioxane) mixture at 298.15 K
- Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
- Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents: IV. Alkylamines in 1,4-dioxane and oxolane at 303.15K
- Excess Molar Enthalpies for Binary and Ternary Mixtures containing Cyclic Ether, 2-Methylaniline and Aromatic Hydrocarbons
- Solubility and Saturation Apparent Volume of Propranolol Hydrochloride in Some Binary Aqueous Cosolvent Mixtures at 298.15 K
- Solubility of Etoricoxib in Aqueous Solutions of 1,4-Butanediol, 1,4-Dioxane, N,N-Dimethylacetamide, N,N-Dimethylformamide, Dimethyl Sulfoxide, and Ethanol at 298.2 K
- Viscous Calibration Liquids for Self-diffusion Measurements
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
- Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
- Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
- Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
- Solubility Correlation and Thermodynamic Analysis of Sorafenib Free Base and Sorafenib Tosylate in Monosolvents and Binary Solvent Mixtures
- Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
- Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
- Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) 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
- Solid-Liquid Equilibrium and Phase Diagram for Ternary 2-Methyl-1,4-naphthoquinone + Phthalic Anhydride +1,4-Dioxane System
- Application of Buffer-Based Ionic Liquid in the Separation of 1,4-Dioxane from Its Azeotropic Aqueous Solution
- Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
- Solubility of Sulfachloropyridazine in Pure and Binary Solvent Mixtures and Investigation of Intermolecular Interactions
- 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
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- Solubility Modeling, Solvent Effect, and Preferential Solvation of Thiamphenicol in Cosolvent Mixtures of Methanol, Ethanol, N,N-Dimethylformamide, and 1,4-Dioxane with Water
- Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
- Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
- Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary Solvents
- Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
- Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
- Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
- Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
- Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
- Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
- Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
- Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
- Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
- Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
- Solid-Liquid Equilibrium of 5-Chloro-8-hydroxyquinoline and 5,7-Dichloro-8-hydroxyquinoline in Different Solvents and Mixing Properties of Solutions
- Solubility Study of (2E)-1-(3-Pyridyl)-3-(dimethylamino)-2-propen-1-one in Different Pure Solvents and Binary Solvent Mixtures from 278.15 to 328.15 K
- Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
- Solubility Determination and Model Correlation of Pymetrozine and Evaluation of the Effect of Solvent Properties and Composition
- Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
- o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
- Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
- Solubility and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
- Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
- Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
- 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
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
- Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
- Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
- Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
- Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
- Solubility of Acetoguanamine in Twelve Neat Solvents from 283.15 to 323.15 K
- Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
- Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
- Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
- Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
- Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
- Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
- Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
- Isothermal Vapor-Liquid Equilibrium Data for the Systems 1,4-Dioxane + Water + Tetrabutylammonium Nitrate and Acetonitrile + Water + Tetrabutylammonium Bromide
- Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K
- Thermodynamic Properties of Water + Tetrahydrofuran and Water + 1,4-Dioxane Mixtures at (303.15, 313.15, and 323.15) K
- Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
- 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
- Excess Molar Enthalpies of Ternary Mixtures of Ethanol + 1-Propanol + Tetrahydropyran or 1,4-Dioxane at 298.15 K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
- Densities, Viscosities, and Sound Speeds of Some Acetate Salts in Binary Mixtures of Tetrahydrofuran and Methanol at (303.15, 313.15, and 323.15) K
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
- Solubility of Benzoic Acid in Mixed Solvents
- Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Solubility of Form III Piracetam in a Range of Solvents
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Different Organic Solvents
- Measurement and Correlation for Solubility of 11alpha-Hydroxy-16alpha,17alpha-epoxyprogesterone and 16alpha,17alpha-Epoxyprogesterone in Solvents
- Critical Assessment of CO2 Solubility in Volatile Solvents at 298.15 K
- Solubilities of Phloretin in 12 Solvents at Different Temperatures
- Partial Molar Volumes and Viscosity B-Coefficients of N,N'-Ethylene-bis(salicylideneiminato)cobalt(II) in Binary Mixtures of 1,4-Dioxane + Methanol at T = (298.15, 303.15, 308.15, and 313.15) K
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Solubility and Phase Separation of 2-(N-Morpholino)ethanesulfonic Acid (MES) and 4-(N-Morpholino)butanesulfonic Acid (MOBS) in Aqueous 1,4-Dioxane and Ethanol Solutions
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Solubility of the Metastable Polymorph of Piracetam (Form II) in a Range of Solvents
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Liquid - Liquid Equilibria for the Ternary Systems of Per fl uorohexane + Methyl Nona fl uorobutyl Ether + Toluene, + 1,4-Dioxane, or + Dimethylformamide at 298.15 K
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Solubility Measurement and Modeling for 2-Benzoyl-3-chlorobenzoic Acid and 1-Chloroanthraquinone in Organic Solvents
- Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
- Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
- Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
- Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
- Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
- Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, 1,4-Dioxane and Piperidine) or (Cyclohexane, Morpholine and Piperidine) at 308.15 K and Atmospheric Pressure
- Measurement of Solid Liquid Phase Equilibrium for the Ternary 3-Nitrophthalic Anhydride + 4-Nitrophthalic Anhydride + 1,4-Dioxane System
- 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
- Solubility and Thermodynamic Functions of Isatin in Pure Solvents
- Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
- Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
- Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
- Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
- Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
- Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
- Ion-Pair and Triple-Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of 1,4-Dioxane + Tetrahydrofuran
- Vapor Pressures for 1,4-Dioxane + Tetrabutylammonium Nitrate, Water + Tetrabutylammonium Nitrate, and 1,4-Dioxane + Water + Tetrabutylammonium Nitrate
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
- Salt Effect on the Enthalpy of Mixing of 1,4-Dioxane + Formic Acid at 303.15 K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent
- KCl-Induced Phase Separation of 1,4-Dioxane + Water Mixtures Studied by Electrical Conductivity and Refractive Index
- Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Solubility of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Organic Solvents and Solubility of 3-Chlorophthalic Acid and 4-Chlorophthalic Acid in Water from (283.15 to 333.15) K
- Excess Molar Enthalpies for the Binary and Ternary Mixtures of Cyclohexane, Tetrahydropyran, and 1,4-Dioxane at 308.15 K and Atmospheric Pressure: Experimental Measurements and Correlations
- Surface Tension and Surface Properties of Binary Mixtures of 1,4-Dioxane or N,N-Dimethyl Formamide with n-Alkyl Acetates
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Transport Properties in 1,4-Dioxane + Water + Saturated KCl Critical Mixture by Measuring Viscosity and Electrical Conductivity
- Liquid-Liquid Equilibrium for the System Water + 1,4-Dioxane + 2,6-Dimethyloct-7-en-2-ol over the Temperature Range of (343.2 to 358.2) K
- Solubility of Biologically Active Chalcones in 1,4-Dioxane and N,N-Dimethyl Formamide from (298.15 to 318.15) K
- Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Micellar Properties and Related Thermodynamic Parameters of the 14-6-14, 2Br- Gemini Surfactant in Water + Organic Solvent Mixed Media
- Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, Tetrahydropyran, and Morpholine) or (Cyclohexane, 1,4-Dioxane, and Morpholine) at 308.15 K and Atmospheric Pressure
- Joback Method
- KDB
- 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.