- InChI
- InChI=1S/C2H6OS/c1-4(2)3/h1-2H3
- InChI Key
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N
- Formula
- C2H6OS
- SMILES
- CS(C)=O
- Molecular Weight1
- 78.13
- CAS
- 67-68-5
- Other Names
-
- (CH3)2SO
- A 10846
- DEMSODROX
- DMS 70
- DMS 90
- DMSO
- DMSO (methyl sulfoxide)
- Deltan
- Demasorb
- Demavet
- Demeso
- Dermasorb
- Dimethyl sulfur oxide
- Dimethyl sulphoxide
- Dimexide
- Dipirartril-tropico
- Dolicur
- Doligur
- Domoso
- Dromisol
- Durasorb
- Gamasol 90
- Herpid
- Hyadur
- Infiltrina
- Kemsol
- M 176
- Methane, 1,1'-sulfinylbis-
- Methane, sulfinylbis-
- Methyl sulfoxide
- Methylsulfinylmethane
- NSC-763
- Rimso 50
- SQ 9453
- SULFINYLBISMETHANE
- Sclerosol
- Somipront
- Sulfoxide, dimethyl
- Sulphinylbis methane
- Syntexan
- Topsym
- PAff : Proton affinity (kJ/mol).
- 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).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- σcond : Electrical conductivity (S/m).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- 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.
- D*i : Self diffusion coefficient (m2/s).
- 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).
- λ : Liquid thermal conductivity (W/m×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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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 884.40 | kJ/mol | NIST |
| BasG | 853.70 | kJ/mol | NIST |
| ΔcH°liquid | -2037.30 ± 1.30 | kJ/mol | NIST |
| EA | [0.01; 0.01] | eV |
|
| EA | 0.01 ± 0.00 | eV | NIST |
| EA | 0.01 | eV | NIST |
| ΔfG° | -251.75 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -150.50 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | -203.40 ± 1.40 | kJ/mol | NIST |
| ΔfusH° | 8.69 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [52.90; 52.90] | kJ/mol |
|
| ΔvapH° | 52.90 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 52.90 ± 0.40 | kJ/mol | NIST |
| IE | [9.01; 9.90] | eV |
|
| IE | 9.10 | eV | NIST |
| IE | 9.08 ± 0.09 | eV | NIST |
| IE | 9.20 ± 0.05 | eV | NIST |
| IE | 9.20 | eV | NIST |
| IE | Outlier 9.90 ± 0.10 | eV | NIST |
| IE | 9.10 | eV | NIST |
| IE | 9.01 | eV | NIST |
| IE | 9.11 | eV | NIST |
| IE | 9.01 | eV | NIST |
| log10WS | 0.70 | Crippen Calculated Property | |
| logPoct/wat | -0.005 | Crippen Calculated Property | |
| McVol | 61.260 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 5704.58 | kPa | Joback Calculated Property |
| Inp | [772.00; 829.20] |
|
|
| Inp | 780.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 777.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 820.10 | NIST | |
| Inp | 820.50 | NIST | |
| Inp | Outlier 829.20 | NIST | |
| Inp | 786.60 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 780.00 | NIST | |
| I | [1549.00; 1603.00] |
|
|
| I | 1569.00 | NIST | |
| I | 1584.00 | NIST | |
| I | 1569.10 | NIST | |
| I | 1560.00 | NIST | |
| I | 1560.00 | NIST | |
| I | 1563.00 | NIST | |
| I | 1582.30 | NIST | |
| I | Outlier 1603.00 | NIST | |
| I | 1582.00 | NIST | |
| I | 1560.00 | NIST | |
| I | 1569.00 | NIST | |
| I | 1596.00 | NIST | |
| I | 1560.00 | NIST | |
| I | 1553.00 | NIST | |
| I | 1595.00 | NIST | |
| I | 1576.00 | NIST | |
| I | 1582.00 | NIST | |
| I | 1553.00 | NIST | |
| I | 1549.00 | NIST | |
| I | 1550.00 | NIST | |
| I | 1579.00 | NIST | |
| I | 1554.00 | NIST | |
| S°liquid | 188.78 | J/mol×K | NIST |
| Tboil | [461.92; 463.85] | K |
|
| Tboil | 461.92 | K | Vapor l... |
| Tboil | 462.18 | K | Isobari... |
| Tboil | 462.24 | K | Experim... |
| Tboil | 462.19 | K | Excess ... |
| Tboil | 463.27 | K | Isobari... |
| Tboil | 463.17 | K | Experim... |
| Tboil | 462.19 | K | Excess ... |
| Tboil | 463.38 | K | Vapor L... |
| Tboil | Outlier 463.85 | K | Isobari... |
| Tboil | 462.06 | K | Vapor-L... |
| Tboil | 462.25 | K | Isobari... |
| Tboil | 462.19 | K | Isobari... |
| Tc | 718.00 | K | Critica... |
| Tfus | [290.95; 291.66] | K |
|
| Tfus | 290.95 | K | Efficie... |
| Tfus | 291.66 | K | Phase E... |
| Tfus | 291.65 ± 0.40 | K | NIST |
| Tfus | 291.57 ± 0.20 | K | NIST |
| Tfus | 291.65 ± 0.20 | K | NIST |
| Ttriple | [291.59; 291.67] | K |
|
| Ttriple | 291.67 | K | KDB |
| Ttriple | 291.59 ± 0.10 | K | NIST |
| Ttriple | 291.67 ± 0.06 | K | NIST |
| Vc | 0.237 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [86.68; 116.06] | J/mol×K | [303.44; 478.96] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 85 90 95 100 105 110 115 300 350 400 450 | ||||
| Cp,gas | 86.68 | J/mol×K | 303.44 | Joback Calculated Property |
| Cp,gas | 91.87 | J/mol×K | 332.69 | Joback Calculated Property |
| Cp,gas | 96.95 | J/mol×K | 361.95 | Joback Calculated Property |
| Cp,gas | 101.92 | J/mol×K | 391.20 | Joback Calculated Property |
| Cp,gas | 106.76 | J/mol×K | 420.45 | Joback Calculated Property |
| Cp,gas | 111.48 | J/mol×K | 449.71 | Joback Calculated Property |
| Cp,gas | 116.06 | J/mol×K | 478.96 | Joback Calculated Property |
| Cp,liquid | [145.00; 172.20] | J/mol×K | [288.15; 423.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 145 150 155 160 165 170 300 350 400 | ||||
| Cp,liquid | 149.90 | J/mol×K | 288.15 | Molar H... |
| Cp,liquid | 146.80 | J/mol×K | 288.15 | Excess ... |
| Cp,liquid | 151.20 | J/mol×K | 293.15 | Thermop... |
| Cp,liquid | 145.00 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 150.40 | J/mol×K | 293.15 | Molar H... |
| Cp,liquid | 149.39 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 152.40 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 151.50 | J/mol×K | 298.15 | Molar H... |
| Cp,liquid | 145.40 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 152.40 | J/mol×K | 298.15 | Thermop... |
| Cp,liquid | 153.18 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 155.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 155.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 153.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 153.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 148.28 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 149.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 146.70 | J/mol×K | 303.15 | Excess ... |
| Cp,liquid | 152.20 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 153.40 | J/mol×K | 303.15 | Thermop... |
| Cp,liquid | 154.60 | J/mol×K | 308.15 | Excess ... |
| Cp,liquid | 152.90 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 148.50 | J/mol×K | 308.15 | Excess ... |
| Cp,liquid | 154.80 | J/mol×K | 308.15 | Thermop... |
| Cp,liquid | 153.70 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 155.40 | J/mol×K | 313.15 | Thermop... |
| Cp,liquid | 149.40 | J/mol×K | 313.15 | Excess ... |
| Cp,liquid | 150.30 | J/mol×K | 318.15 | Excess ... |
| Cp,liquid | 156.60 | J/mol×K | 318.15 | Thermop... |
| Cp,liquid | 154.70 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 157.70 | J/mol×K | 323.15 | Thermop... |
| Cp,liquid | 151.50 | J/mol×K | 323.15 | Excess ... |
| Cp,liquid | 155.60 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 157.80 | J/mol×K | 328.15 | Thermop... |
| Cp,liquid | 152.60 | J/mol×K | 328.15 | Excess ... |
| Cp,liquid | 158.50 | J/mol×K | 333.15 | Thermop... |
| Cp,liquid | 154.10 | J/mol×K | 333.15 | Excess ... |
| Cp,liquid | 155.30 | J/mol×K | 338.15 | Excess ... |
| Cp,liquid | 159.30 | J/mol×K | 338.15 | Thermop... |
| Cp,liquid | 156.80 | J/mol×K | 343.15 | Excess ... |
| Cp,liquid | 159.50 | J/mol×K | 343.15 | Thermop... |
| Cp,liquid | 160.20 | J/mol×K | 348.15 | Thermop... |
| Cp,liquid | 158.20 | J/mol×K | 348.15 | Excess ... |
| Cp,liquid | 159.60 | J/mol×K | 353.15 | Excess ... |
| Cp,liquid | 160.30 | J/mol×K | 353.15 | Thermop... |
| Cp,liquid | 161.30 | J/mol×K | 358.15 | Thermop... |
| Cp,liquid | 160.60 | J/mol×K | 358.15 | Excess ... |
| Cp,liquid | 161.50 | J/mol×K | 363.15 | Thermop... |
| Cp,liquid | 160.90 | J/mol×K | 363.15 | Excess ... |
| Cp,liquid | 161.30 | J/mol×K | 368.15 | Excess ... |
| Cp,liquid | 161.70 | J/mol×K | 368.15 | Thermop... |
| Cp,liquid | 161.70 | J/mol×K | 373.15 | Excess ... |
| Cp,liquid | 162.60 | J/mol×K | 373.15 | Thermop... |
| Cp,liquid | 161.80 | J/mol×K | 378.15 | Excess ... |
| Cp,liquid | 163.30 | J/mol×K | 378.15 | Thermop... |
| Cp,liquid | 164.80 | J/mol×K | 383.15 | Thermop... |
| Cp,liquid | 162.70 | J/mol×K | 383.15 | Excess ... |
| Cp,liquid | 163.80 | J/mol×K | 388.15 | Excess ... |
| Cp,liquid | 166.30 | J/mol×K | 388.15 | Thermop... |
| Cp,liquid | 164.20 | J/mol×K | 393.15 | Excess ... |
| Cp,liquid | 168.30 | J/mol×K | 393.15 | Thermop... |
| Cp,liquid | 165.30 | J/mol×K | 398.15 | Excess ... |
| Cp,liquid | 169.10 | J/mol×K | 398.15 | Thermop... |
| Cp,liquid | 170.30 | J/mol×K | 403.15 | Thermop... |
| Cp,liquid | 166.60 | J/mol×K | 403.15 | Excess ... |
| Cp,liquid | 167.40 | J/mol×K | 408.15 | Excess ... |
| Cp,liquid | 170.40 | J/mol×K | 408.15 | Thermop... |
| Cp,liquid | 170.60 | J/mol×K | 413.15 | Thermop... |
| Cp,liquid | 168.10 | J/mol×K | 413.15 | Excess ... |
| Cp,liquid | 171.10 | J/mol×K | 418.15 | Thermop... |
| Cp,liquid | 169.00 | J/mol×K | 418.15 | Excess ... |
| Cp,liquid | 172.20 | J/mol×K | 423.15 | Excess ... |
| Cp,liquid | 171.20 | J/mol×K | 423.15 | Thermop... |
| η | [0.0008500; 0.0022100] | Pa×s | [293.15; 353.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 1.80e-3 2.00e-3 2.20e-3 300 320 340 | ||||
| η | 0.0022100 | Pa×s | 293.15 | Viscosi... |
| η | 0.0022100 | Pa×s | 293.15 | Viscosi... |
| η | 0.0020420 | Pa×s | 298.15 | Viscosi... |
| η | 0.0019660 | Pa×s | 298.15 | Densiti... |
| η | 0.0019890 | Pa×s | 298.15 | Excess ... |
| η | 0.0019960 | Pa×s | 298.15 | Density... |
| η | 0.0020120 | Pa×s | 298.15 | Viscosi... |
| η | 0.0020418 | Pa×s | 298.15 | Densiti... |
| η | 0.0019790 | Pa×s | 298.15 | Volumet... |
| η | 0.0019960 | Pa×s | 298.15 | On the ... |
| η | 0.0020120 | Pa×s | 298.15 | Propert... |
| η | 0.0019932 | Pa×s | 298.15 | Partial... |
| η | 0.0020100 | Pa×s | 298.15 | Viscosi... |
| η | 0.0018430 | Pa×s | 303.15 | Propert... |
| η | 0.0018006 | Pa×s | 303.15 | Partial... |
| η | 0.0017860 | Pa×s | 303.15 | Densiti... |
| η | 0.0018320 | Pa×s | 303.15 | Densiti... |
| η | 0.0018400 | Pa×s | 303.15 | Viscosi... |
| η | 0.0018357 | Pa×s | 303.15 | Density... |
| η | 0.0018090 | Pa×s | 303.15 | Densiti... |
| η | 0.0018357 | Pa×s | 303.15 | On the ... |
| η | 0.0018430 | Pa×s | 303.15 | Viscosi... |
| η | 0.0016520 | Pa×s | 308.15 | Partial... |
| η | 0.0016689 | Pa×s | 308.15 | On the ... |
| η | 0.0016523 | Pa×s | 308.15 | Densiti... |
| η | 0.0016220 | Pa×s | 308.15 | Volumet... |
| η | 0.0015682 | Pa×s | 308.15 | Densiti... |
| η | 0.0016550 | Pa×s | 308.15 | THERMOD... |
| η | 0.0016689 | Pa×s | 308.15 | Density... |
| η | 0.0016696 | Pa×s | 308.15 | Densiti... |
| η | 0.0016450 | Pa×s | 308.15 | Excess ... |
| η | 0.0015680 | Pa×s | 308.15 | Viscosi... |
| η | 0.0015373 | Pa×s | 313.15 | Densiti... |
| η | 0.0015060 | Pa×s | 313.15 | Densiti... |
| η | 0.0015560 | Pa×s | 313.15 | Viscosi... |
| η | 0.0015351 | Pa×s | 313.15 | Density... |
| η | 0.0015588 | Pa×s | 313.15 | Densiti... |
| η | 0.0015160 | Pa×s | 313.15 | Partial... |
| η | 0.0015351 | Pa×s | 313.15 | On the ... |
| η | 0.0015560 | Pa×s | 313.15 | Propert... |
| η | 0.0015600 | Pa×s | 313.15 | Viscosi... |
| η | 0.0014875 | Pa×s | 318.15 | Densiti... |
| η | 0.0013920 | Pa×s | 318.15 | THERMOD... |
| η | 0.0013814 | Pa×s | 318.15 | Volumet... |
| η | 0.0013935 | Pa×s | 318.15 | On the ... |
| η | 0.0013935 | Pa×s | 318.15 | Density... |
| η | 0.0014850 | Pa×s | 318.15 | Viscosi... |
| η | 0.0014847 | Pa×s | 318.15 | Densiti... |
| η | 0.0014080 | Pa×s | 318.15 | Densiti... |
| η | 0.0013980 | Pa×s | 318.15 | Partial... |
| η | 0.0013370 | Pa×s | 323.15 | Propert... |
| η | 0.0013370 | Pa×s | 323.15 | Viscosi... |
| η | 0.0012890 | Pa×s | 323.15 | Densiti... |
| η | 0.0013400 | Pa×s | 323.15 | Viscosi... |
| η | 0.0012780 | Pa×s | 323.15 | Densiti... |
| η | 0.0012070 | Pa×s | 328.15 | Volumet... |
| η | 0.0011700 | Pa×s | 333.15 | Viscosi... |
| η | 0.0011650 | Pa×s | 333.15 | Viscosi... |
| η | 0.0011040 | Pa×s | 333.15 | Densiti... |
| η | 0.0011650 | Pa×s | 333.15 | Propert... |
| η | 0.0010300 | Pa×s | 343.15 | Viscosi... |
| η | 0.0010280 | Pa×s | 343.15 | Viscosi... |
| η | 0.0010280 | Pa×s | 343.15 | Propert... |
| η | 0.0009620 | Pa×s | 343.15 | Densiti... |
| η | 0.0008500 | Pa×s | 353.15 | Densiti... |
| η | 0.0009200 | Pa×s | 353.15 | Viscosi... |
| η | 0.0009170 | Pa×s | 353.15 | Propert... |
| η | 0.0009170 | Pa×s | 353.15 | Viscosi... |
| σcond | [1.88e-04; 4.74e-04] | S/m | [293.15; 333.15] |
|
|
T(K) Electrical conductivity (S/m) 2.00e-4 2.50e-4 3.00e-4 3.50e-4 4.00e-4 4.50e-4 5.00e-4 300 310 320 330 | ||||
| σcond | 1.88e-04 | S/m | 293.15 | Tempera... |
| σcond | 2.01e-04 | S/m | 295.15 | Tempera... |
| σcond | 2.11e-04 | S/m | 297.15 | Tempera... |
| σcond | 2.25e-04 | S/m | 299.15 | Tempera... |
| σcond | 2.36e-04 | S/m | 301.15 | Tempera... |
| σcond | 2.48e-04 | S/m | 303.15 | Tempera... |
| σcond | 2.62e-04 | S/m | 305.15 | Tempera... |
| σcond | 2.74e-04 | S/m | 307.15 | Tempera... |
| σcond | 2.87e-04 | S/m | 309.15 | Tempera... |
| σcond | 3.00e-04 | S/m | 311.15 | Tempera... |
| σcond | 3.15e-04 | S/m | 313.15 | Tempera... |
| σcond | 3.28e-04 | S/m | 315.15 | Tempera... |
| σcond | 3.41e-04 | S/m | 317.15 | Tempera... |
| σcond | 3.55e-04 | S/m | 319.15 | Tempera... |
| σcond | 3.69e-04 | S/m | 321.15 | Tempera... |
| σcond | 3.84e-04 | S/m | 323.15 | Tempera... |
| σcond | 3.99e-04 | S/m | 325.15 | Tempera... |
| σcond | 4.19e-04 | S/m | 327.15 | Tempera... |
| σcond | 4.37e-04 | S/m | 329.15 | Tempera... |
| σcond | 4.55e-04 | S/m | 331.15 | Tempera... |
| σcond | 4.74e-04 | S/m | 333.15 | Tempera... |
| ΔfusH | [14.37; 14.37] | kJ/mol | [291.67; 291.70] |
|
| ΔfusH | 14.37 | kJ/mol | 291.67 | NIST |
| ΔfusH | 14.37 | kJ/mol | 291.70 | NIST |
| ΔfusH | 14.37 | kJ/mol | 291.70 | NIST |
| ΔvapH | [48.10; 52.50] | kJ/mol | [308.00; 430.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 48 49 50 51 52 350 400 | ||||
| ΔvapH | 52.50 | kJ/mol | 308.00 | NIST |
| ΔvapH | 52.30 | kJ/mol | 308.00 | NIST |
| ΔvapH | 52.10 | kJ/mol | 363.00 | NIST |
| ΔvapH | 48.10 | kJ/mol | 368.00 | NIST |
| ΔvapH | 50.60 | kJ/mol | 383.50 | NIST |
| ΔvapH | 51.70 | kJ/mol | 384.50 | NIST |
| ΔvapH | 48.60 | kJ/mol | 430.00 | NIST |
| Pvap | [0.06; 101.30] | kPa | [293.15; 463.38] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 450 | ||||
| Pvap | 0.06 | kPa | 293.15 | Recomme... |
| Pvap | 0.06 | kPa | 293.15 | Recomme... |
| Pvap | 0.06 | kPa | 293.15 | Recomme... |
| Pvap | 0.07 | kPa | 295.65 | Recomme... |
| Pvap | 0.07 | kPa | 295.65 | Recomme... |
| Pvap | 0.07 | kPa | 295.65 | Recomme... |
| Pvap | 0.08 | kPa | 298.15 | Recomme... |
| Pvap | 0.08 | kPa | 298.15 | Recomme... |
| Pvap | 0.08 | kPa | 298.15 | Recomme... |
| Pvap | 0.10 | kPa | 300.65 | Recomme... |
| Pvap | 0.10 | kPa | 300.65 | Recomme... |
| Pvap | 0.10 | kPa | 300.65 | Recomme... |
| Pvap | 0.11 | kPa | 303.16 | Recomme... |
| Pvap | 0.11 | kPa | 303.16 | Recomme... |
| Pvap | 0.11 | kPa | 303.16 | Recomme... |
| Pvap | 0.13 | kPa | 305.66 | Recomme... |
| Pvap | 0.13 | kPa | 305.66 | Recomme... |
| Pvap | 0.13 | kPa | 305.66 | Recomme... |
| Pvap | 0.16 | kPa | 308.16 | Recomme... |
| Pvap | 0.16 | kPa | 308.16 | Recomme... |
| Pvap | 0.16 | kPa | 308.16 | Recomme... |
| Pvap | 2.00 | kPa | 353.10 | Determi... |
| Pvap | 3.20 | kPa | 363.10 | Determi... |
| Pvap | 5.00 | kPa | 373.10 | Determi... |
| Pvap | 7.60 | kPa | 383.10 | Determi... |
| Pvap | 11.20 | kPa | 393.10 | Determi... |
| Pvap | 16.00 | kPa | 403.10 | Determi... |
| Pvap | 22.70 | kPa | 413.10 | Determi... |
| Pvap | 31.60 | kPa | 423.10 | Determi... |
| Pvap | 43.20 | kPa | 433.10 | Determi... |
| Pvap | 95.30 | kPa | 460.95 | Vapor-l... |
| Pvap | 101.30 | kPa | 463.27 | Isobari... |
| Pvap | 101.30 | kPa | 463.38 | Vapor L... |
| n0 | [1.45470; 1.47930] | [288.15; 318.15] |
|
|
|
T(K) Refractive Index 1.45 1.46 1.47 1.47 1.48 1.48 290 300 310 | ||||
| n0 | 1.47930 | 288.15 | Partial... | |
| n0 | 1.47850 | 293.15 | Densiti... | |
| n0 | 1.47850 | 293.15 | Experim... | |
| n0 | 1.47910 | 293.15 | Solid-L... | |
| n0 | 1.47890 | 293.15 | Solubil... | |
| n0 | 1.47510 | 293.15 | Isobari... | |
| n0 | 1.47520 | 298.15 | Partial... | |
| n0 | 1.47680 | 298.15 | Density... | |
| n0 | 1.47690 | 298.15 | Viscosi... | |
| n0 | 1.47790 | 298.15 | Isobari... | |
| n0 | 1.45940 | 303.15 | Density... | |
| n0 | 1.47510 | 303.15 | Measure... | |
| n0 | 1.47100 | 308.15 | Partial... | |
| n0 | 1.45470 | 308.15 | Density... | |
| n0 | 1.46700 | 318.15 | Partial... | |
| ρl | [1019.80; 1101.20] | kg/m3 | [293.14; 373.15] |
|
|
T(K) Liquid Density (kg/m3) 1020 1040 1060 1080 1100 300 320 340 360 | ||||
| ρl | 1100.87 | kg/m3 | 293.14 | Volumet... |
| ρl | 1100.40 | kg/m3 | 293.15 | Volumet... |
| ρl | 1100.22 | kg/m3 | 293.15 | Thermod... |
| ρl | 1100.23 | kg/m3 | 293.15 | Thermod... |
| ρl | 1100.00 | kg/m3 | 293.15 | Thermop... |
| ρl | 1100.40 | kg/m3 | 293.15 | Experim... |
| ρl | 1100.20 | kg/m3 | 293.15 | Excess ... |
| ρl | 1100.43 | kg/m3 | 293.15 | Thermod... |
| ρl | 1100.43 | kg/m3 | 293.15 | Thermod... |
| ρl | 1100.41 | kg/m3 | 293.15 | Apparen... |
| ρl | 1100.42 | kg/m3 | 293.15 | Carbon ... |
| ρl | 1100.31 | kg/m3 | 293.15 | Volumet... |
| ρl | 1101.20 | kg/m3 | 293.15 | Determi... |
| ρl | 1100.22 | kg/m3 | 293.15 | Apparen... |
| ρl | 1100.00 | kg/m3 | 293.15 | Volumet... |
| ρl | 1100.42 | kg/m3 | 293.15 | Molar C... |
| ρl | 1100.20 | kg/m3 | 293.15 | Density... |
| ρl | 1100.76 | kg/m3 | 293.15 | Volumet... |
| ρl | 1100.22 | kg/m3 | 293.15 | Apparen... |
| ρl | 1095.40 | kg/m3 | 298.15 | Experim... |
| ρl | 1095.36 | kg/m3 | 298.15 | Densiti... |
| ρl | 1095.33 | kg/m3 | 298.15 | Tempera... |
| ρl | 1095.40 | kg/m3 | 298.15 | Isobari... |
| ρl | 1095.30 | kg/m3 | 298.15 | Conduct... |
| ρl | 1095.45 | kg/m3 | 298.15 | Molar C... |
| ρl | 1095.27 | kg/m3 | 298.15 | Volumet... |
| ρl | 1095.00 | kg/m3 | 298.15 | Volumet... |
| ρl | 1096.02 | kg/m3 | 298.15 | Physics... |
| ρl | 1096.50 | kg/m3 | 298.15 | Thermop... |
| ρl | 1095.19 | kg/m3 | 298.15 | Apparen... |
| ρl | 1095.32 | kg/m3 | 298.15 | Excess ... |
| ρl | 1095.20 | kg/m3 | 298.15 | Solubil... |
| ρl | 1095.54 | kg/m3 | 298.15 | Excess ... |
| ρl | 1095.37 | kg/m3 | 298.15 | Influen... |
| ρl | 1095.28 | kg/m3 | 298.15 | Density... |
| ρl | 1095.37 | kg/m3 | 298.15 | Excess ... |
| ρl | 1095.27 | kg/m3 | 298.15 | Volumet... |
| ρl | 1095.74 | kg/m3 | 298.15 | Volumet... |
| ρl | 1095.42 | kg/m3 | 298.15 | Thermod... |
| ρl | 1095.41 | kg/m3 | 298.15 | Carbon ... |
| ρl | 1095.20 | kg/m3 | 298.15 | Excess ... |
| ρl | 1096.00 | kg/m3 | 298.15 | Probing... |
| ρl | 1095.28 | kg/m3 | 298.15 | Solvati... |
| ρl | 1095.42 | kg/m3 | 298.15 | Thermod... |
| ρl | 1095.37 | kg/m3 | 298.15 | Effect ... |
| ρl | 1095.19 | kg/m3 | 298.15 | Thermod... |
| ρl | 1095.39 | kg/m3 | 298.15 | Apparen... |
| ρl | 1095.25 | kg/m3 | 298.15 | Solvati... |
| ρl | 1095.30 | kg/m3 | 298.15 | Volumet... |
| ρl | 1095.20 | kg/m3 | 298.15 | Thermod... |
| ρl | 1096.80 | kg/m3 | 298.15 | Excess ... |
| ρl | 1095.20 | kg/m3 | 298.15 | Thermod... |
| ρl | 1095.19 | kg/m3 | 298.15 | Thermod... |
| ρl | 1095.34 | kg/m3 | 298.15 | Liquid-... |
| ρl | 1090.31 | kg/m3 | 303.13 | Volumet... |
| ρl | 1090.81 | kg/m3 | 303.15 | Volumet... |
| ρl | 1090.18 | kg/m3 | 303.15 | Thermod... |
| ρl | 1090.26 | kg/m3 | 303.15 | Solvati... |
| ρl | 1090.00 | kg/m3 | 303.15 | Thermop... |
| ρl | 1090.47 | kg/m3 | 303.15 | Molar C... |
| ρl | 1090.29 | kg/m3 | 303.15 | Effect ... |
| ρl | 1090.38 | kg/m3 | 303.15 | Carbon ... |
| ρl | 1090.41 | kg/m3 | 303.15 | Thermod... |
| ρl | 1090.29 | kg/m3 | 303.15 | Influen... |
| ρl | 1090.34 | kg/m3 | 303.15 | Apparen... |
| ρl | 1090.36 | kg/m3 | 303.15 | Apparen... |
| ρl | 1090.41 | kg/m3 | 303.15 | Density... |
| ρl | 1092.41 | kg/m3 | 303.15 | Influen... |
| ρl | 1091.40 | kg/m3 | 303.15 | Excess ... |
| ρl | 1090.24 | kg/m3 | 303.15 | Solvati... |
| ρl | 1090.17 | kg/m3 | 303.15 | Thermod... |
| ρl | 1090.30 | kg/m3 | 303.15 | Thermop... |
| ρl | 1090.00 | kg/m3 | 303.15 | Volumet... |
| ρl | 1090.38 | kg/m3 | 303.15 | Apparen... |
| ρl | 1091.20 | kg/m3 | 303.15 | Determi... |
| ρl | 1090.45 | kg/m3 | 303.15 | Excess ... |
| ρl | 1090.20 | kg/m3 | 303.15 | Density... |
| ρl | 1090.32 | kg/m3 | 303.15 | Tempera... |
| ρl | 1090.16 | kg/m3 | 303.15 | Apparen... |
| ρl | 1092.41 | kg/m3 | 303.15 | Effect ... |
| ρl | 1090.73 | kg/m3 | 303.15 | Volumet... |
| ρl | 1090.60 | kg/m3 | 303.15 | Solubil... |
| ρl | 1090.40 | kg/m3 | 303.15 | Thermod... |
| ρl | 1090.37 | kg/m3 | 303.15 | Apparen... |
| ρl | 1090.37 | kg/m3 | 303.15 | Apparen... |
| ρl | 1090.20 | kg/m3 | 303.15 | Excess ... |
| ρl | 1085.27 | kg/m3 | 308.15 | Volumet... |
| ρl | 1085.35 | kg/m3 | 308.15 | Apparen... |
| ρl | 1085.90 | kg/m3 | 308.15 | Solubil... |
| ρl | 1086.06 | kg/m3 | 308.15 | Effect ... |
| ρl | 1085.31 | kg/m3 | 308.15 | Tempera... |
| ρl | 1085.50 | kg/m3 | 308.15 | Excess ... |
| ρl | 1085.24 | kg/m3 | 308.15 | Solvati... |
| ρl | 1086.10 | kg/m3 | 308.15 | Excess ... |
| ρl | 1085.42 | kg/m3 | 308.15 | Apparen... |
| ρl | 1085.20 | kg/m3 | 308.15 | Thermop... |
| ρl | 1085.48 | kg/m3 | 308.15 | Molar C... |
| ρl | 1085.23 | kg/m3 | 308.15 | Density... |
| ρl | 1085.36 | kg/m3 | 308.15 | Densiti... |
| ρl | 1086.08 | kg/m3 | 308.15 | Effect ... |
| ρl | 1086.06 | kg/m3 | 308.15 | Influen... |
| ρl | 1085.28 | kg/m3 | 308.15 | Influen... |
| ρl | 1085.39 | kg/m3 | 308.15 | Thermod... |
| ρl | 1085.41 | kg/m3 | 308.15 | Apparen... |
| ρl | 1085.23 | kg/m3 | 308.15 | Solvati... |
| ρl | 1085.28 | kg/m3 | 308.15 | Effect ... |
| ρl | 1085.36 | kg/m3 | 308.15 | Carbon ... |
| ρl | 1085.39 | kg/m3 | 308.15 | Thermod... |
| ρl | 1080.77 | kg/m3 | 313.14 | Volumet... |
| ρl | 1080.43 | kg/m3 | 313.15 | Apparen... |
| ρl | 1080.00 | kg/m3 | 313.15 | Thermop... |
| ρl | 1080.20 | kg/m3 | 313.15 | Excess ... |
| ρl | 1080.29 | kg/m3 | 313.15 | Tempera... |
| ρl | 1080.30 | kg/m3 | 313.15 | Effect ... |
| ρl | 1080.69 | kg/m3 | 313.15 | Volumet... |
| ρl | 1080.22 | kg/m3 | 313.15 | Solvati... |
| ρl | 1080.33 | kg/m3 | 313.15 | Apparen... |
| ρl | 1080.20 | kg/m3 | 313.15 | Solvati... |
| ρl | 1081.43 | kg/m3 | 313.15 | Influen... |
| ρl | 1080.27 | kg/m3 | 313.15 | Volumet... |
| ρl | 1080.30 | kg/m3 | 313.15 | Influen... |
| ρl | 1080.40 | kg/m3 | 313.15 | Density... |
| ρl | 1080.37 | kg/m3 | 313.15 | Density... |
| ρl | 1080.12 | kg/m3 | 313.15 | Apparen... |
| ρl | 1080.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 1080.12 | kg/m3 | 313.15 | Thermod... |
| ρl | 1080.49 | kg/m3 | 313.15 | Molar C... |
| ρl | 1080.34 | kg/m3 | 313.15 | Carbon ... |
| ρl | 1080.20 | kg/m3 | 313.15 | Thermop... |
| ρl | 1081.30 | kg/m3 | 313.15 | Solubil... |
| ρl | 1081.20 | kg/m3 | 313.15 | Excess ... |
| ρl | 1081.10 | kg/m3 | 313.15 | Determi... |
| ρl | 1080.47 | kg/m3 | 313.15 | Apparen... |
| ρl | 1080.30 | kg/m3 | 313.15 | Experim... |
| ρl | 1080.45 | kg/m3 | 313.15 | Apparen... |
| ρl | 1080.12 | kg/m3 | 313.15 | Thermod... |
| ρl | 1075.30 | kg/m3 | 318.15 | Solubil... |
| ρl | 1075.30 | kg/m3 | 318.15 | Excess ... |
| ρl | 1075.49 | kg/m3 | 318.15 | Molar C... |
| ρl | 1076.30 | kg/m3 | 318.15 | Thermop... |
| ρl | 1075.19 | kg/m3 | 318.15 | Density... |
| ρl | 1075.31 | kg/m3 | 318.15 | Influen... |
| ρl | 1075.31 | kg/m3 | 318.15 | Apparen... |
| ρl | 1075.31 | kg/m3 | 318.15 | Effect ... |
| ρl | 1075.21 | kg/m3 | 318.15 | Solvati... |
| ρl | 1075.18 | kg/m3 | 318.15 | Solvati... |
| ρl | 1075.32 | kg/m3 | 318.15 | Carbon ... |
| ρl | 1070.73 | kg/m3 | 323.14 | Volumet... |
| ρl | 1070.32 | kg/m3 | 323.15 | Effect ... |
| ρl | 1070.20 | kg/m3 | 323.15 | Density... |
| ρl | 1070.29 | kg/m3 | 323.15 | Apparen... |
| ρl | 1070.00 | kg/m3 | 323.15 | Volumet... |
| ρl | 1071.10 | kg/m3 | 323.15 | Determi... |
| ρl | 1070.07 | kg/m3 | 323.15 | Apparen... |
| ρl | 1070.08 | kg/m3 | 323.15 | Thermod... |
| ρl | 1070.33 | kg/m3 | 323.15 | Density... |
| ρl | 1070.28 | kg/m3 | 323.15 | Densiti... |
| ρl | 1070.32 | kg/m3 | 323.15 | Influen... |
| ρl | 1070.66 | kg/m3 | 323.15 | Volumet... |
| ρl | 1070.08 | kg/m3 | 323.15 | Thermod... |
| ρl | 1070.31 | kg/m3 | 323.15 | Carbon ... |
| ρl | 1065.33 | kg/m3 | 328.15 | Influen... |
| ρl | 1065.26 | kg/m3 | 328.15 | Apparen... |
| ρl | 1065.33 | kg/m3 | 328.15 | Effect ... |
| ρl | 1065.14 | kg/m3 | 328.15 | Solvati... |
| ρl | 1065.29 | kg/m3 | 328.15 | Carbon ... |
| ρl | 1060.68 | kg/m3 | 333.15 | Volumet... |
| ρl | 1060.34 | kg/m3 | 333.15 | Effect ... |
| ρl | 1060.28 | kg/m3 | 333.15 | Carbon ... |
| ρl | 1060.63 | kg/m3 | 333.15 | Volumet... |
| ρl | 1060.04 | kg/m3 | 333.15 | Thermod... |
| ρl | 1060.03 | kg/m3 | 333.15 | Apparen... |
| ρl | 1060.34 | kg/m3 | 333.15 | Influen... |
| ρl | 1060.20 | kg/m3 | 333.15 | Experim... |
| ρl | 1061.20 | kg/m3 | 333.15 | Determi... |
| ρl | 1060.30 | kg/m3 | 333.15 | Density... |
| ρl | 1060.29 | kg/m3 | 333.15 | Density... |
| ρl | 1060.03 | kg/m3 | 333.15 | Thermod... |
| ρl | 1055.34 | kg/m3 | 338.15 | Influen... |
| ρl | 1055.26 | kg/m3 | 338.15 | Carbon ... |
| ρl | 1055.34 | kg/m3 | 338.15 | Effect ... |
| ρl | 1050.62 | kg/m3 | 343.14 | Volumet... |
| ρl | 1050.35 | kg/m3 | 343.15 | Influen... |
| ρl | 1050.20 | kg/m3 | 343.15 | Density... |
| ρl | 1050.35 | kg/m3 | 343.15 | Effect ... |
| ρl | 1050.58 | kg/m3 | 343.15 | Volumet... |
| ρl | 1051.30 | kg/m3 | 343.15 | Determi... |
| ρl | 1050.23 | kg/m3 | 343.15 | Carbon ... |
| ρl | 1045.21 | kg/m3 | 348.15 | Carbon ... |
| ρl | 1045.34 | kg/m3 | 348.15 | Influen... |
| ρl | 1045.34 | kg/m3 | 348.15 | Effect ... |
| ρl | 1040.54 | kg/m3 | 353.14 | Volumet... |
| ρl | 1040.33 | kg/m3 | 353.15 | Influen... |
| ρl | 1040.19 | kg/m3 | 353.15 | Carbon ... |
| ρl | 1041.10 | kg/m3 | 353.15 | Determi... |
| ρl | 1040.20 | kg/m3 | 353.15 | Density... |
| ρl | 1040.33 | kg/m3 | 353.15 | Effect ... |
| ρl | 1040.51 | kg/m3 | 353.15 | Volumet... |
| ρl | 1035.15 | kg/m3 | 358.15 | Carbon ... |
| ρl | 1030.43 | kg/m3 | 363.15 | Volumet... |
| ρl | 1031.30 | kg/m3 | 363.15 | Determi... |
| ρl | 1029.90 | kg/m3 | 363.15 | Density... |
| ρl | 1030.12 | kg/m3 | 363.15 | Carbon ... |
| ρl | 1021.40 | kg/m3 | 373.15 | Determi... |
| ρl | 1019.80 | kg/m3 | 373.15 | Density... |
| D*i | [0.00; 0.00] | m2/s | [293.09; 363.71] |
|
|
T(K) Self diffusion coefficient (m2/s) 5.00e-10 1.00e-9 1.50e-9 2.00e-9 300 320 340 360 | ||||
| D*i | 0.00 | m2/s | 293.09 | Viscous... |
| D*i | 0.00 | m2/s | 298.26 | Viscous... |
| D*i | 0.00 | m2/s | 298.29 | Viscous... |
| D*i | 0.00 | m2/s | 308.10 | Viscous... |
| D*i | 0.00 | m2/s | 318.03 | Viscous... |
| D*i | 0.00 | m2/s | 328.10 | Viscous... |
| D*i | 0.00 | m2/s | 338.12 | Viscous... |
| D*i | 0.00 | m2/s | 348.17 | Viscous... |
| D*i | 0.00 | m2/s | 363.71 | Viscous... |
| ΔfusS | 49.26 | J/mol×K | 291.67 | NIST |
| csound,fluid | [1451.47; 1519.12] | m/s | [288.15; 308.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1450 1460 1470 1480 1490 1500 1510 1520 290 295 300 305 | ||||
| csound,fluid | 1519.12 | m/s | 288.15 | Volumet... |
| csound,fluid | 1502.19 | m/s | 293.15 | Volumet... |
| csound,fluid | 1485.21 | m/s | 298.15 | Volumet... |
| csound,fluid | 1484.12 | m/s | 298.15 | Adiabat... |
| csound,fluid | 1468.32 | m/s | 303.15 | Volumet... |
| csound,fluid | 1451.47 | m/s | 308.15 | Volumet... |
| γ | [0.04; 0.04] | N/m | [288.15; 328.15] |
|
|
T(K) Surface Tension (N/m) 0.04 0.04 0.04 0.04 0.04 0.04 0.04 290 300 310 320 | ||||
| γ | 0.04 | N/m | 288.15 | Study o... |
| γ | 0.04 | N/m | 293.15 | Thermod... |
| γ | 0.04 | N/m | 298.15 | Surface... |
| γ | 0.04 | N/m | 298.15 | Effect ... |
| γ | 0.04 | N/m | 298.15 | Equilib... |
| γ | 0.04 | N/m | 298.15 | Thermod... |
| γ | 0.04 | N/m | 298.15 | Study o... |
| γ | 0.04 | N/m | 298.15 | Surface... |
| γ | 0.04 | N/m | 303.15 | Thermod... |
| γ | 0.04 | N/m | 303.15 | Surface... |
| γ | 0.04 | N/m | 303.15 | Surface... |
| γ | 0.04 | N/m | 308.15 | Effect ... |
| γ | 0.04 | N/m | 308.15 | Thermod... |
| γ | 0.04 | N/m | 308.15 | Surface... |
| γ | 0.04 | N/m | 308.15 | Surface... |
| γ | 0.04 | N/m | 308.15 | Equilib... |
| γ | 0.04 | N/m | 308.15 | Study o... |
| γ | 0.04 | N/m | 313.15 | Surface... |
| γ | 0.04 | N/m | 313.15 | Surface... |
| γ | 0.04 | N/m | 313.15 | Thermod... |
| γ | 0.04 | N/m | 318.15 | Effect ... |
| γ | 0.04 | N/m | 318.15 | Equilib... |
| γ | 0.04 | N/m | 318.15 | Study o... |
| γ | 0.04 | N/m | 318.15 | Surface... |
| γ | 0.04 | N/m | 323.15 | Surface... |
| γ | 0.04 | N/m | 328.15 | Equilib... |
| γ | 0.04 | N/m | 328.15 | Study o... |
| γ | 0.04 | N/m | 328.15 | Effect ... |
| γ | 0.04 | N/m | 328.15 | Surface... |
| λ | [0.18; 0.19] | W/m×K | [294.83; 339.35] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.18 0.18 0.18 0.18 0.18 0.19 0.19 300 320 340 | ||||
| λ | 0.19 | W/m×K | 294.83 | Thermal... |
| λ | 0.19 | W/m×K | 299.84 | Thermal... |
| λ | 0.18 | W/m×K | 304.64 | Thermal... |
| λ | 0.18 | W/m×K | 309.47 | Thermal... |
| λ | 0.18 | W/m×K | 314.33 | Thermal... |
| λ | 0.18 | W/m×K | 319.33 | Thermal... |
| λ | 0.18 | W/m×K | 324.37 | Thermal... |
| λ | 0.18 | W/m×K | 329.31 | Thermal... |
| λ | 0.18 | W/m×K | 334.49 | Thermal... |
| λ | 0.18 | W/m×K | 339.35 | Thermal... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [461.55; 462.19] | K | [95.30; 96.60] |
|
| Tboil | 462.19 | K | 95.30 | Excess ... |
| Tboil | 461.55 | K | 96.60 | Low cos... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 101.00 | 303.15 | 0.0018 |
| Reference | ||
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 85.90 | 298.15 | 1.4762 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 81.50 | 298.15 | 1.4767 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 85.90 | 298.15 | 1095.29 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.05; 353.23] | kPa | [291.67; 519.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.67806e+01 | |||
| Coefficient B | -7.52281e+03 | |||
| Coefficient C | -4.21562e+00 | |||
| Coefficient D | -2.45086e-07 | |||
| Temperature range, min. | 291.67 | |||
| Temperature range, max. | 519.15 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 300 400 500 | ||||
| Pvap | 0.05 | kPa | 291.67 | Calculated Property |
| Pvap | 0.28 | kPa | 316.95 | Calculated Property |
| Pvap | 1.18 | kPa | 342.22 | Calculated Property |
| Pvap | 3.96 | kPa | 367.50 | Calculated Property |
| Pvap | 11.12 | kPa | 392.77 | Calculated Property |
| Pvap | 27.08 | kPa | 418.05 | Calculated Property |
| Pvap | 58.68 | kPa | 443.32 | Calculated Property |
| Pvap | 115.36 | kPa | 468.60 | Calculated Property |
| Pvap | 208.97 | kPa | 493.87 | Calculated Property |
| Pvap | 353.23 | kPa | 519.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Dimethyl Sulfoxide.
Mixtures
- 1-Butanol + Dimethyl Sulfoxide
- Dimethyl Sulfoxide + 1-Hexanol
- Toluene + Dimethyl Sulfoxide
- Ethylbenzene + Dimethyl Sulfoxide
- Benzene, chloro- + Dimethyl Sulfoxide
- Benzene, bromo- + Dimethyl Sulfoxide
- Benzene, nitro- + Dimethyl Sulfoxide
- Dimethyl Sulfoxide + Water
- Acetic acid + Dimethyl Sulfoxide
- Acetic acid + Dimethyl Sulfoxide + Water
- Benzenamine, 4,4'-oxybis- + Dimethyl Sulfoxide
- Ethanol, 2-methoxy- + Dimethyl Sulfoxide
- Toluene + Ethanol, 2-methoxy- + Dimethyl Sulfoxide
- Dimethyl Sulfoxide + Acetic acid, methyl ester
- Dimethyl Sulfoxide + Methyl Alcohol
- Dimethyl Sulfoxide + Acetic acid, methyl ester + Methyl Alcohol
- Dimethyl Sulfoxide + o-Xylene
- Benzene, 1,3-dimethyl- + Dimethyl Sulfoxide
- p-Xylene + Dimethyl Sulfoxide
- Styrene + Dimethyl Sulfoxide
Find more mixtures with Dimethyl Sulfoxide.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
- Volumetric Properties of the Ionic Liquid, 1-Butyl-3-methylimidazolium Tetrafluoroborate, in Organic Solvents at T = 298.15 K
- Volumetric and Isentropic Compressibility Behavior of Ionic Liquid, 1-Propyl-3-Methylimidazolium Bromide in Acetonitrile, Dimethylformamide, and Dimethylsulfoxide at T = (288.15 to 308.15) K
- Solubility of sodium diclofenac in different solvents
- Solubility of disperse yellow 54 in supercritical carbon dioxide with or without cosolvent
- Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
- Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
- Vapor liquid equilibria for water + acetic acid + (N,N-dimethylformamide or dimethyl sulfoxide) at 13.33 kPa
- Volumetric properties of ionic liquid 1,3-dimethylimidazolium methyl sulfate + molecular solvents at T = (298.15 - 328.15) K
- The solid-liquid equilibrium of the binary system H2O-DMSO and the influence of a salt (NaCl, KCl) on the thermodynamic behavior Correlations using a revised LIQUAC model
- Recommended vapor pressures for thiophene, sulfolane, and dimethyl sulfoxide
- Conductivity is a contrivance to explore ion-pair and triple-ion structure of ethanoates in tetrahydrofuran, dimethyl sulfoxide and their binaries
- Effect of solvent on the volumetric behavior ofN,N' -salicylidenephenyl diamine (Salophen) Schiff base at differenttemperatures (288.15 - 318.15) K
- Measurement and correlation of the solubility of 4,4'-oxydianiline in different organic solvents
- Spectroscopic and ultrasonic studies on the molecular interaction of certain aromatic amines with p-chloranil
- Experimental solubility of hydrogen sulfide and carbon dioxide in dimethylformamide and dimethylsulfoxide
- Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
- Apparent molar volumes and isentropic compressions of benzylalkylammonium ionic liquids in dimethylsulfoxide from 293.15 K to 328.15 K
- Temperature dependent solubility of sodium cyclamate in selected pure solvents and binary methanol + water mixed solvents
- Absorption, desorption and spectroscopic investigation of sulfur dioxide in the binary system ethylene glycol + dimethyl sulfoxide
- Experimental isobaric vapor-liquid equilibrium for the ternary system of sec-butyl alcohol + sec-butyl acetate + dimethyl sulfoxide at 101.3 kPa
- Experimental isobaric vapor-liquid equilibrium for the binary and ternary systems with methanol, methyl acetate and dimethyl sulfoxide at 101.3 kPa
- Experimental isobaric (vapor + liquid) equilibrium data for the binary system N, N-dimethyl formamide + dimethyl sulfoxide and the quaternary system sec-butyl alcohol + sec-butyl acetate + N, Ndimethyl formamide + dimethyl sulfoxide at 101.3 kPa
- Phase equilibria of ternary systems of carbon dioxide + ethanol, dimethyl sulfoxide, or N,N-dimethyl formamide + water at elevated pressures including near critical regions
- Solubilities of six lithium salts in five non-aqueous solvents and in a few of their binary mixtures
- 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
- Critical temperatures and pressures of caprolactam, dimethyl sulfoxide, 1,4-dimethylpiperazine, and 2,6-dimethylpiperazine
- New vapour-liquid equilibrium data on the ternary system carbon dioxide - methanol - dimethyl sulphoxide
- Densities and volumetric properties of a (xylene + dimethyl sulfoxide) at temperature from (293.15 to 353.15) K
- Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
- Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
- Partial molar volumes of L-alanine, DL-serine, DL-threonine, L-histidine, glycine, and glycylglycine in water, NaCl, and DMSO aqueous solutions at T = 298.15 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
- Volumetric and compressibility behaviour of ionic liquid, 1-n-butyl-3-methylimidazolium hexafluorophosphate and tetrabutylammonium hexafluorophosphate in organic solvents at T = 298.15 K
- Adiabatic compressibility of pseudo-binary aqueous solutions of tert-butyl alcohol and dimethylsulfoxide as a result of ultrasonic investigations
- Volumetric, ultrasonic and viscometric studies of binary mixtures of dimethyl sulphoxide with chloro and nitro substituted aromatic hydrocarbons at T = 303.15 K
- Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
- On the density and viscosity of (water + dimethylsulphoxide) binary mixtures
- Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
- Thermodynamic studies of some non-electrolytes in aqueous solutions at low temperatures
- 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
- Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
- Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
- Conductometric study of some alkali metal halides in (dimethyl sulfoxide + acetonitrile) at T = 298.15 K
- Surface and bulk behavior of (dialkylsulfoxides + carbon tetrachloride) mixtures
- Effect of temperature on volumetric and viscometric properties of some non-steroidal anti-inflammatory drugs in aprotic solvents
- Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
- Apparent molar volumes and compressibilities of alkaline earth metal ions in methanol and dimethylsulfoxide
- Apparent molar volumes and compressibilities of selected electrolytes in dimethylsulfoxide
- Experimental and predicted refractive index properties in ternary mixtures of associated liquids
- Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
- Effects of clustering structure on volumetric properties of amino acids in (DMSO + water) mixtures
- Apparent molar volumes and compressibilities of lanthanum, gadolinium and lutetium trifluoromethanesulfonates in dimethylsulfoxide
- Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
- Physics and chemistry of an ionic liquid in some industrially important solvent media probed by physicochemical techniques
- Thermophysical and excess properties of hydroxamic acids in DMSO
- Influence of anion on thermophysical properties of ionic liquids with polar solvent
- Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
- Thermodynamic surface properties of [BMIm][NTf2] or [EMIm][NTf2] binary mixtures with tetrahydrofuran, acetonitrile or dimethylsulfoxide
- Probing subsistence of ion-pair and triple-ion of an ionic salt in liquid environments by means of conductometric contrivance
- Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
- Effect of ionic liquid on the solvation behavior of nonaqueous N,N'-salicylidenephenylediamine Schiff base (Salophen) solutions at 298.15 K
- Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
- (Liquid + liquid) equilibria for (benzene + cyclohexane + dimethyl sulfoxide) system at T = (298.15 or 303.15) K: Experimental data and correlation
- Solvation of ionic liquids based on N-methyl-N-alkyl morpholinium cations in dimethylsulfoxide - volumetric and compressibility studies
- Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
- Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
- Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
- Solvation of ionic liquids based on N-alkyl-N-methylmorpholinium cations in N,N-dimethylformamide and dimethyl sulfoxide A volumetric and acoustic study
- Excess molar volume and viscosity deviation for binary mixtures of gamma-butyrolactone with dimethyl sulfoxide
- Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
- Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
- Effect of organic solvents on lowering the viscosity of 1-hexyl-3- methylimidazolium chloride
- Equilibrium solubility, dissolution thermodynamics and preferential solvation of adenosine in aqueous solutions of N,N-dimethylformamide, N-methyl-2-pyrrolidone, dimethylsulfoxide and propylene glycol
- Equilibrium solubility, dissolution thermodynamics and preferential solvation of 6-methyl-2-thiouracil in aqueous co-solvent mixtures of methanol, N-methyl-2-pyrrolidone, N,N-dimethyl formamide and dimethylsulfoxide
- Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
- Temperature and composition dependence of the volumetric and acoustic properties of ionic liquid [emim][HSO4] with polar protic and aprotic co-solvents
- Determination of density, viscosity and vapor pressures of mixtures of dimethyl sulfoxide + 1-allyl-3-methylimidazolium chloride at atmospheric pressure
- Solubility of l-tyrosine in aqueous solutions of methanol, ethanol, n-propanol and dimethyl sulfoxide: Experimental determination and preferential solvation analysis
- Solubility modelling and preferential solvation of adenine in solvent mixtures of (N,N-dimethylformamide, N-methyl pyrrolidone, propylene glycol and dimethyl sulfoxide) plus water
- Thermodynamic evidence for nano-heterogeneity in solutions of the macrocycle C-butylresorcin[4]arene in non-aqueous solvents
- Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
- Liquid-liquid equilibria and density data for pseudoternary systems of refined soybean oil + (hexanal, or heptanal, or butyric acid, or valeric acid, or caproic acid, or caprylic acid) + dimethyl sulfoxide at 298.15 K
- Experimental solubility evaluation and thermodynamic analysis of quinocetone in aqueous co-solvent solutions of ethanol, isopropanol, dimethyl sulfoxide and N,N-dimethylformamide
- The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
- Equilibrium solubility determination, modelling and preferential solvation of bioactive iminodibenzyl in aqueous co-solvent mixtures at various temperatures
- Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
- Equilibrium solubility investigation and thermodynamic aspects of biologically active gimeracil (form P) dissolved in aqueous co-solvent mixtures of isopropanol, N,N-dimethylformamide, ethylene glycol and dimethylsulfoxide
- Thermodynamic solubility modelling, solvent effect and preferential solvation of naftopidil in aqueous co-solvent solutions of (n-propanol, ethanol, isopropanol and dimethyl sulfoxide)
- 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
- Isobaric vapor-liquid equilibrium of a ternary system of ethyl acetate + propyl acetate + dimethyl sulfoxide and binary systems of ethyl acetate + dimethyl sulfoxide and propyl acetate + dimethyl sulfoxide at 101.3 kPa
- Solubility and preferential solvation of flubendazole dissolved in aqueous co-solvent mixtures of 1,4-dioxane, dimethyl sulfoxide, N,N-dimethylformamide and isopropanol
- Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide + dimethyl sulfoxide) and the quaternary system (sec-butyl acetate + sec-butyl alcohol + N, N-dimethyl acetamide + dimethyl sulfoxide) at 101.3 kPa
- Thermodynamic solubility modelling, solvent effect and preferential solvation of p-nitrobenzamide in aqueous co-solvent mixtures of dimethyl sulfoxide, ethanol, isopropanol and ethylene glycol
- 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
- Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
- Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
- Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
- Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
- THERMODYNAMIC INTERACTIONS OF POTASSIUM FLUORIDE IN AQUEOUS DIMETHYL SULFOXIDE SOLUTIONS AT DIFFERENT TEMPERATURES
- Enthalpic Pairwise Interactions of Isomers of 2,4-pentanediol and 2,5-hexanediol in Dimethylsulfoxide + Water Mixtures at 298.15 K
- Effect of anion variation on the thermophysical properties of triethylammonium based protic ionic liquids with polar solvent
- Probing molecular interactions of ionic liquid in industrially important solvents by means of conductometric and spectroscopic approach
- Conductometric, refractometric and FT-IR spectroscopic study of [EMIm]NO3, [EMIm]CH3SO3, and [EMIm]OTs in N,N-dimethyl formamide, N,N-dimethyl acetamide and dimethyl sulphoxide
- Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
- Apparent thermodynamic analysis and the dissolution behavior of levamisole hydrochloride in three binary solvent mixtures
- Solubility of 3,7-Dinitro-1,3,5,7-tetraazabicyclo [3.3.1] Nonane in Ethanenitrile, Methanol, 1,1-Dichloroethane, Dimethyl Sulfoxide, Acetone, and Mixed Solvents
- 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
- Excess Properties and Spectroscopic Studies for Binary System of Polyethylene Glycol 200 (1) + Dimethyl Sulfoxide (2) at T = (298.15 to 318.15) K
- Viscous Calibration Liquids for Self-diffusion Measurements
- Density, sound speed and viscosity of dihydropyridine derivatives in dimethyl sulfoxide at different temperatures
- Measurement and Correlation of the Solubility of Sodium 2- Chlorotoluene-4-sulfonate in Selected Pure Solvents and Aqueous Organic Solutions
- Density and Viscosity Measurements for Binary Mixtures of 1-Ethyl-3-methylimidazolium Tetrafluoroborate ([Emim][BF4]) with Dimethylacetamide, Dimethylformamide, and Dimethyl Sulfoxide
- Solubility and Spectral Studies for SO2 in Binary System of Tri-ethylene Glycol + Dimethyl Sulfoxide at T = (298.15, 303.15, and 308.15) K and p = 123.15 kPa
- Solubilities of Dihydroxylammonium 5,5'-Bistetrazole-1,1'-diolate in Various Pure Solvents at Temperatures Between 293.15 and 323.15 K
- Vapor Liquid Equilibria for Ternary Mixtures of Isopropyl Alcohol, Isopropyl Acetate, and DMSO at 101.3 kPa
- Solubility Properties and Absorption Mechanism Investigation of Dilute SO2 in Propylene Glycol Monomethyl Ether + Dimethyl Sulfoxide System
- Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
- Carbon Dioxide Solubility in Phosphonium-, Ammonium-, Sulfonyl-, and Pyrrolidinium-Based Ionic Liquids and their Mixtures at Moderate Pressures up to 10 bar
- Influence of Aprotic Cosolvents on the Thermophysical Properties of Imidazolium-Based Ionic Liquid
- Isobaric Vapor Liquid Equilibrium for the Binary and Ternary System with Isobutyl Alcohol, Isobutyl Acetate and Dimethyl Sulfoxide at 101.3 kPa
- Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
- Excess Molar Volumes, Excess Molar Isentropic Compressibilities, Viscosity Deviations, and Activation Parameters for 1-Ethyl-3-methyl-imidazolium Trifluoro-methanesulfonate + Dimethyl Sulfoxide and/or Acetonitrile at T = 298.15 to 323.15 K and P = 0.1 MPa
- Determination of Density and Viscosity of Binary Mixtures of Water and Dimethyl Sulfoxide with 1-Ethyl-3-methylimidazolium Diethylphosphate [EtMeIm]+[Et2PO4]- at Atmospheric Pressure
- Solubility and Preferential Solvation of Carbazochrome in Solvent Mixtures of N,N-Dimethylformamide Plus Methanol/Ethanol/n-Propanol and Dimethyl Sulfoxide Plus Water
- Solubility of Ionic Liquid [Bmim]Ac in Supercritical CO2 Containing Different Cosolvents
- Measurement and Correlation of the Solubility of Florfenicol Form A in Several Pure and Binary Solvents
- Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
- Effect of Cosolvents DMSO and Glycerol on the Self-Assembly Behavior of SDBS and CPC: An Experimental and Theoretical Approach
- Viscosities of 1-Hexyl-3-methylimidazolium Tetrafluoroborate and Its Binary Mixtures with Dimethyl Sulfoxide and Acetonitrile
- The Dependence of Temperature and Composition on the Equilibrium Solubility and Thermodynamic Studies of Bioactive N-(9-Fluorenylmethoxycarbonyloxy)succinimide in Various Water-Cosolvent Mixtures
- Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
- Density and Melting Points for the Binary Mixtures Dimethyl Sulfoxide (DMSO) + 1-Ethyl-3-methylimidazolium Acetate and DMSO + Choline Acetate
- Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
- 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
- Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
- Solubility Determination and Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
- Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
- Propylthiouracil Solubility in Aqueous Solutions of Ethylene Glycol, N,N-Dimethylformamide, N-Methyl-2-pyrrolidone, and Dimethylsulfoxide: Measurement and Thermodynamic Modeling
- Domperidone Solubility in Aqueous Cosolvent Mixtures of N,N-Dimethylformamide, Isopropanol, Dimethyl Sulfoxide, and Ethanol: Thermodynamic Modeling and Preferential Solvation Analysis
- Solubility Determination and Model Correlation of Pymetrozine and Evaluation of the Effect of Solvent Properties and Composition
- Solubility of d-Tryptophan and l-Tyrosine in Several Organic Solvents: Determination and Solvent Effect
- 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
- Solubility and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
- Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
- Experimental High-Temperature, High-Pressure Density Measurement and Perturbed-Chain Statistical Associating Fluid Theory Modeling of Dimethyl Sulfoxide, Isoamyl Acetate, and Benzyl Alcohol
- Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
- Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
- Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
- Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
- Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
- Liquid-Liquid Equilibria of Water + Benzonitrile + Propanone, or + Dimethylsulfoxide
- Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
- Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
- Solubilities of Terephthalic Acid in Dimethyl Sulfoxide + Water and in N,N-Dimethylformamide + Water from (301.4 to 373.7) 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 volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
- Excess Enthalpies of {CH3(CH2)nCN, n = 5 to 12} + Methyl Methylthiomethyl Sulfoxide or + Dimethyl Sulfoxide at 298.15 K
- Excess Enthalpies, Heat Capacities, Densities, Viscosities and Refractive Indices of Dimethyl Sulfoxide + Three Aryl Alcohols at 308.15 K and Atmospheric Pressure
- Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
- 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
- Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
- Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + 1-Propanol at (288.15, 298.15, and 308.15) K and at Normal Pressure
- Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
- Vapor-Liquid Equilibria for the Ternary System Acetonitrile + 1-Propanol + Dimethyl Sulfoxide and the Corresponding Binary Systems at 101.3 kPa
- Densities and Volumetric Properties of Ethylene Glycol + Dimethylsulfoxide Mixtures at Temperatures of (278.15 to 323.15) K and Pressures of (0.1 to 100) MPa
- Ion Association and Solvation of Sulfathiazole Sodium in Aqueous and Partial Aqueous Media
- Volumetric Properties of Binary Mixtures Containing Ionic Liquids and Some Aprotic Solvents
- Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
- 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
- Densities and Viscosities for Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetrafluoroborate Ionic Liquid with Molecular Solvents
- Enthalpies of Dilution of 1,3-Propanediol and Isomers of 2,3-Butanediol in Dimethylsulfoxide + Water Mixtures at 298.15 K
- Osmolality and Unfrozen Water Content of Aqueous Solution of Dimethyl Sulfoxide
- Apparent Molar Volumes and Expansivities of Ionic Liquids [Cnmim]Br (n = 4, 8, 10, 12) in Dimethyl Sulfoxide
- Volumetric Properties of Binary Mixtures of Two 1-Alkyl-3-Methylimidazolium Tetrafluoroborate Ionic Liquids with Molecular Solvents
- Properties of Pure 1-Butyl-2,3-dimethylimidazolium Tetrafluoroborate Ionic Liquid and Its Binary Mixtures with Dimethyl Sulfoxide and Acetonitrile
- Thermal Conductivity of DMSO + C2H5OH, DMSO + H2O, and DMSO + C2H5OH + H2O Mixtures at T = (278.15 to 338.15) K
- Solubilities of Octahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine in ?-Butyrolactone + Water, Dimethylsulfoxide + Water, and N-Methyl pyrrolidone + Water
- Temperature and Concentration Dependences of the Electric Conductivity of Dimethyl Sulfoxide + Ammonium Nitrate Electrolytes
- Isobaric Vapor Liquid Equilibrium for the Extractive Distillation of Acetonitrile + Water Mixtures Using Dimethyl Sulfoxide at 101.3 kPa
- Isobaric Vapor Liquid Equilibrium of Binary and Ternary Systems with 2-Ethoxyethanol + Ethylbenzene + Dimethyl Sulfoxide
- Electrical Conductivity in Dimethyl Sulfoxide + Potassium Iodide Solutions at Different Concentrations and Temperatures
- Solubility of Dilute SO2 in the Binary System Poly Ethylene Glycol 300 + Dimethyl Sulfoxide at T = 298.15 K and p = 123.15 kPa and Mixtures Excess Properties at T = (298.15, 303.15, 308.15, 313.15, and 318.15) K
- Determination and Correlation of Solubilities of Lithium Bis(oxalate)borate in Six Different Solvents from (293.15 to 363.15) K
- Solubilities of 1,1'-[1,2-Ethanediylbis(oxy-1,2-ethanediyl)]bis-[3-methyl-1H-imidazolium-1-yl] Dihexafluorophosphate in Water, Methanol, Ethanol, Dimethylformamide, Dimethyl Sulfoxide, and (Acetone + Water) Binary Solvent Mixtures
- Dilution Enthalpies and Enthalpic Pairwise Self-Interactions of Nicotinamide and Isonicotinamide in (Dimethylformamide + Water) and (Dimethylsulfoxide + Water) Mixed Solvents at 298.15 K
- Phase Equilibrium, Excess Enthalpies and Densities of Binary Mixtures of Trimethylbutylammonium Bis(trifluoromethylsulfonyl)imide with Ethanol, 1-Propanol and Dimethylformamide
- Experimental Measurement and Modeling of the Solubility of Biotin in Six Pure Solvents at Temperatures from 298.15 K to 333.85 K
- Solubility and Solvation Thermodynamics of a Series of Homologous a-Amino Acids in Nonaqueous Binary Mixtures of Ethylene Glycol and Dimethyl Sulfoxide
- Isothermal Vapor-Liquid Equilibria of Binary Mixtures of Nitrogen with Dimethyl Sulfoxide, N-Methyl-2-pyrrolidone, and Diethylene Glycol Monobutyl Ether at Elevated Pressures
- Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Tetrahydropyran and + 2-Methyltetrahydrofuran at (293.15, 303.15, and 313.15) K
- Solubility of Sodium Cefotaxime in Different Solvents
- Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
- Surface Tension and Refractive Index of Dialkylsulfoxide + Water Mixtures at Several Temperatures
- Viscosity, Density, Speed of Sound, and Refractive Index of Binary Mixtures of Organic Solvent + Ionic Liquid, 1-Butyl-3-methylimidazolium Hexafluorophosphate at 298.15 K
- Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
- Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
- Densities and Volumetric Properties of Binary and Ternary Liquid Mixtures of Water (1) + Acetonitrile (2) + Dimethyl Sulfoxide (3) at Temperatures from (293.15 to 333.15) K and at Ambient Pressure (81.5 kPa)
- Partial Molar Volumes and Viscosity B-Coefficient of N-Phenylbenzohydroxamic Acid in Dimethylsulfoxide at Different Temperatures
- Densities and Viscosities of N,N-Dimethylformamide + N-Methyl-2-pyrrolidinone and + Dimethyl Sulfoxide in the Temperature Range (303.15 to 353.15) K
- Density and Viscosity of Anhydrous Mixtures of Dimethylsulfoxide with Acetonitrile in the Range (298.15 to 318.15) K
- Solubility of Clindamycin Phosphate in Methanol, Ethanol, and Dimethyl Sulfoxide
- Liquid-Liquid Equilibria of Ternary Systems Sulfide + Octane + Solvents at Different Temperatures
- Solubility of C.I. Disperse Violet 1 in Supercritical Carbon Dioxide with or without Cosolvent
- Adiabatic Compressibilities of Divalent Transition-Metal Perchlorates and Chlorides in N,N-Dimethylacetamide and Dimethylsulfoxide
- Conductivities of Binary Mixtures of Ionic Liquids with Polar Solvents
- Solubility of 1,5-Diaminobromo-4,8-dihydroxyanthraquinone in Supercritical Carbon Dioxide with or without Cosolvent
- Solubility of Tobramycin in Methanol, Ethanol, Dimethyl Sulfoxide, and N,N-Dimethylformamide
- Solubility of l-Lysine Hydrochloride in Dimethyl Sulfoxide, Methanol, Ethanol, Water, and Glycol between (283 and 323) K
- Densities and Viscosities of Rubidium Bromide in Dimethyl Sulfoxide + Water Mixtures in the Temperature Range t = (25 to 45) deg C
- Apparent Molar Volumes and Electrical Conductance of Ionic Liquids [Cnmim]Br (n = 8, 10, 12) in Ethylene Glycol, N,N-Dimethylformamide, and Dimethylsulfoxide at 298.15 K
- Solubility of 1,1-Diamino-2,2-dinitroethylene in N,N-Dimethylformamide, Dimethyl Sulfoxide, and N-Methyl-2-pyrrolidone
- Solubility of 2,6-Diamino-3,5-dinitropyridine and 2,5-Dihydroxyterephthalic Acid in N,N-Dimethylformamide, Dimethylsulfoxide, Ethanol, and Methanol, N,N-Dimethylacetamide, and Acetic Acid
- Solubilities of 1,1'-(Propane-1,3-diyl)-bis(pyridinium) Dihexafluorophosphate in Dimethyl Sulfoxide + Water
- Molar Conductivities and Association Constants of 1-Butyl-3-methylimidazolium Chloride and 1-Butyl-3-methylimidazolium Tetrafluoroborate in Methanol and DMSO
- Enthalpies of Dilution of l-Alanine in Dimethylsulfoxide + Water and Dimethylformamide + Water Mixtures at 298.15 K
- (Liquid + Liquid) Equilibria of (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanone) and (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanol) at T = 303.2 K
- Excess Molar Enthalpies of Dibromomethane with Benzene, Methanol, Dimethylsulfoxide, and Pyrrolidin-2-one at 303.15 K
- Thermodynamic Properties of Inorganic Salts in Nonaqueous Solvents. VI. Apparent Molar Volumes, Expansibilities, and Compressibilities of Divalent Transition Metal Ions in Methanol and Dimethylsulfoxide
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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