- InChI
- InChI=1S/C4H10O2/c1-3(5)4(2)6/h3-6H,1-2H3
- InChI Key
- OWBTYPJTUOEWEK-UHFFFAOYSA-N
- Formula
- C4H10O2
- SMILES
- CC(O)C(C)O
- Molecular Weight1
- 90.12
- CAS
- 513-85-9
- Other Names
-
- 2,3-BUTYLENE GLYCOL
- 2,3-Butandiol
- 2,3-Butanediol, isomer 1
- 2,3-Butanediol, isomer 2
- 2,3-Dihydroxybutane
- 2,3-butanediol, isomer not specified
- 2,3-butanodiol
- 2,3-butyleneglycol
- 2,3-butyleneglycol, isomer not specified
- 2.3-Butanediol, isomer 3
- Butane-2,3-diol
- D-2,3-Butane diol
- DIMETHYLETHYLENE GLYCOL
- butane, 2,3-dihydroxy-, isomer not specified
- 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).
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -2461.00 | kJ/mol | NIST |
| Cp,liquid | 236.63 | J/mol×K | Molar h... |
| ΔfG° | -295.72 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -440.91 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | [-544.80; -541.80] | kJ/mol |
|
| ΔfH°liquid | -544.80 | kJ/mol | NIST |
| ΔfH°liquid | -541.80 | kJ/mol | NIST |
| ΔfusH° | 7.25 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 57.08 | kJ/mol | Joback Calculated Property |
| log10WS | -0.25 | Crippen Calculated Property | |
| logPoct/wat | -0.252 | Crippen Calculated Property | |
| McVol | 78.960 | ml/mol | McGowan Calculated Property |
| Pc | 5087.49 | kPa | Joback Calculated Property |
| Inp | [746.00; 824.00] |
|
|
| Inp | 789.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | Outlier 747.50 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | Outlier 824.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | Outlier 746.00 | NIST | |
| Inp | Outlier 750.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 782.00 | NIST | |
| I | [1492.00; 1590.00] |
|
|
| I | Outlier 1494.00 | NIST | |
| I | Outlier 1492.00 | NIST | |
| I | Outlier 1492.00 | NIST | |
| I | 1522.00 | NIST | |
| I | 1526.00 | NIST | |
| I | 1580.00 | NIST | |
| I | 1545.00 | NIST | |
| I | 1570.00 | NIST | |
| I | 1556.00 | NIST | |
| I | 1542.00 | NIST | |
| I | 1539.00 | NIST | |
| I | 1543.00 | NIST | |
| I | 1547.00 | NIST | |
| I | 1543.00 | NIST | |
| I | 1543.00 | NIST | |
| I | 1541.00 | NIST | |
| I | 1542.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1579.00 | NIST | |
| I | 1558.00 | NIST | |
| I | 1562.00 | NIST | |
| I | 1522.00 | NIST | |
| I | 1541.00 | NIST | |
| I | 1576.00 | NIST | |
| I | 1554.00 | NIST | |
| I | 1580.00 | NIST | |
| I | 1542.00 | NIST | |
| I | 1558.00 | NIST | |
| I | 1523.00 | NIST | |
| I | 1566.00 | NIST | |
| I | 1539.00 | NIST | |
| I | 1539.00 | NIST | |
| I | 1526.00 | NIST | |
| I | 1517.00 | NIST | |
| I | 1512.00 | NIST | |
| I | 1529.00 | NIST | |
| I | 1536.00 | NIST | |
| I | 1590.00 | NIST | |
| I | 1563.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1553.00 | NIST | |
| I | 1581.00 | NIST | |
| I | 1524.00 | NIST | |
| I | 1581.00 | NIST | |
| I | 1550.00 | NIST | |
| I | 1528.00 | NIST | |
| I | 1577.00 | NIST | |
| I | 1521.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1580.00 | NIST | |
| I | 1539.00 | NIST | |
| I | 1541.00 | NIST | |
| I | 1558.00 | NIST | |
| I | 1554.00 | NIST | |
| I | 1566.00 | NIST | |
| I | 1512.00 | NIST | |
| I | Outlier 1494.00 | NIST | |
| I | 1583.00 | NIST | |
| Tboil | [415.15; 456.70] | K |
|
| Tboil | 454.21 | K | Vapor l... |
| Tboil | 454.21 | K | Liquid ... |
| Tboil | 454.21 | K | Liquid ... |
| Tboil | 454.21 | K | Liquid ... |
| Tboil | 456.70 | K | NIST |
| Tboil | 455.65 ± 1.00 | K | NIST |
| Tboil | 455.15 ± 4.00 | K | NIST |
| Tboil | Outlier 415.15 ± 3.00 | K | NIST |
| Tc | 639.26 | K | Joback Calculated Property |
| Tfus | 292.15 ± 2.00 | K | NIST |
| Vc | 0.285 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [173.55; 210.57] | J/mol×K | [474.40; 639.26] |
|
| Cp,gas | 173.55 | J/mol×K | 474.40 | Joback Calculated Property |
| Cp,gas | 180.37 | J/mol×K | 501.88 | Joback Calculated Property |
| Cp,gas | 186.92 | J/mol×K | 529.35 | Joback Calculated Property |
| Cp,gas | 193.21 | J/mol×K | 556.83 | Joback Calculated Property |
| Cp,gas | 199.24 | J/mol×K | 584.30 | Joback Calculated Property |
| Cp,gas | 205.02 | J/mol×K | 611.78 | Joback Calculated Property |
| Cp,gas | 210.57 | J/mol×K | 639.26 | Joback Calculated Property |
| Cp,liquid | [213.00; 262.67] | J/mol×K | [298.15; 353.15] |
|
| Cp,liquid | 236.67 | J/mol×K | 298.15 | Molar h... |
| Cp,liquid | 213.00 | J/mol×K | 298.20 | NIST |
| Cp,liquid | 239.28 | J/mol×K | 303.15 | Molar h... |
| Cp,liquid | 241.85 | J/mol×K | 308.15 | Molar h... |
| Cp,liquid | 244.35 | J/mol×K | 313.15 | Molar h... |
| Cp,liquid | 246.82 | J/mol×K | 318.15 | Molar h... |
| Cp,liquid | 249.23 | J/mol×K | 323.15 | Molar h... |
| Cp,liquid | 251.60 | J/mol×K | 328.15 | Molar h... |
| Cp,liquid | 253.91 | J/mol×K | 333.15 | Molar h... |
| Cp,liquid | 256.17 | J/mol×K | 338.15 | Molar h... |
| Cp,liquid | 258.39 | J/mol×K | 343.15 | Molar h... |
| Cp,liquid | 260.55 | J/mol×K | 348.15 | Molar h... |
| Cp,liquid | 262.67 | J/mol×K | 353.15 | Molar h... |
| η | [0.0001208; 1.9625358] | Pa×s | [226.48; 474.40] |
|
| η | 1.9625358 | Pa×s | 226.48 | Joback Calculated Property |
| η | 0.1120965 | Pa×s | 267.80 | Joback Calculated Property |
| η | 0.0137635 | Pa×s | 309.12 | Joback Calculated Property |
| η | 0.0027712 | Pa×s | 350.44 | Joback Calculated Property |
| η | 0.0007824 | Pa×s | 391.76 | Joback Calculated Property |
| η | 0.0002812 | Pa×s | 433.08 | Joback Calculated Property |
| η | 0.0001208 | Pa×s | 474.40 | Joback Calculated Property |
| ΔvapH | [55.70; 62.50] | kJ/mol | [378.00; 402.50] |
|
| ΔvapH | 57.90 | kJ/mol | 378.00 | NIST |
| ΔvapH | 55.70 | kJ/mol | 379.50 | NIST |
| ΔvapH | 58.40 | kJ/mol | 386.00 | NIST |
| ΔvapH | 62.50 | kJ/mol | 402.50 | NIST |
| n0 | 1.43660 | 298.15 | Densiti... | |
| ρl | [990.72; 990.72] | kg/m3 | [308.15; 308.15] |
|
| ρl | 990.72 | kg/m3 | 308.15 | Effect ... |
| ρl | 990.72 | kg/m3 | 308.15 | A compa... |
| ρl | 990.72 | kg/m3 | 308.15 | Thermod... |
| ρl | 990.72 | kg/m3 | 308.15 | Effect ... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [351.12; 481.36] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.62445e+01 | |||
| Coefficient B | -4.52281e+03 | |||
| Coefficient C | -6.76820e+01 | |||
| Temperature range, min. | 351.12 | |||
| Temperature range, max. | 481.36 | |||
| Pvap | 1.33 | kPa | 351.12 | Calculated Property |
| Pvap | 2.89 | kPa | 365.59 | Calculated Property |
| Pvap | 5.85 | kPa | 380.06 | Calculated Property |
| Pvap | 11.10 | kPa | 394.53 | Calculated Property |
| Pvap | 19.96 | kPa | 409.00 | Calculated Property |
| Pvap | 34.21 | kPa | 423.48 | Calculated Property |
| Pvap | 56.23 | kPa | 437.95 | Calculated Property |
| Pvap | 89.02 | kPa | 452.42 | Calculated Property |
| Pvap | 136.33 | kPa | 466.89 | Calculated Property |
| Pvap | 202.63 | kPa | 481.36 | Calculated Property |
| Pvap | [5.07e-03; 5358.29] | kPa | [280.75; 611.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.37891e+02 | |||
| Coefficient B | -1.22864e+04 | |||
| Coefficient C | -1.78282e+01 | |||
| Coefficient D | 1.38579e-05 | |||
| Temperature range, min. | 280.75 | |||
| Temperature range, max. | 611.00 | |||
| Pvap | 5.07e-03 | kPa | 280.75 | Calculated Property |
| Pvap | 0.12 | kPa | 317.44 | Calculated Property |
| Pvap | 1.34 | kPa | 354.14 | Calculated Property |
| Pvap | 8.74 | kPa | 390.83 | Calculated Property |
| Pvap | 39.74 | kPa | 427.53 | Calculated Property |
| Pvap | 139.69 | kPa | 464.22 | Calculated Property |
| Pvap | 408.58 | kPa | 500.92 | Calculated Property |
| Pvap | 1047.90 | kPa | 537.61 | Calculated Property |
| Pvap | 2448.03 | kPa | 574.31 | Calculated Property |
| Pvap | 5358.29 | kPa | 611.00 | Calculated Property |
Similar Compounds
![2,3-Butanediol, [S-(R*,R*)]-.](data:image/png;base64,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)
Find more compounds similar to 2,3-Butanediol.
Mixtures
- 1-Butanol + 2,3-Butanediol
- Acetic acid, butyl ester + 2,3-Butanediol
- Ethyl Acetate + 2,3-Butanediol
- 1-Butanol + 2,3-Butanediol + Water
- Ethyl Acetate + 2,3-Butanediol + Water
- 2-Pyrrolidinone + 2,3-Butanediol
- Formamide, N,N-dimethyl- + 2,3-Butanediol
- 2-Pyrrolidinone, 1-methyl- + 2,3-Butanediol
- 2,3-Butanediol + Methyl Alcohol
- 2,3-Butanediol + Water
- Acetic acid, butyl ester + 2,3-Butanediol + Water
- Glucose + 2,3-Butanediol + Water
- sodium bromide + 2,3-Butanediol + Water
- 2,3-Butanediol + Water + ammonium bromide
- Tetraethylammonium bromide + 2,3-Butanediol + Water
- 2,3-Butanediol + Glycine + Water
- D-Leucine + 2,3-Butanediol + Water
- L-Asparagine + 2,3-Butanediol + Water
- D-Valine + 2,3-Butanediol + Water
- N-Glycylglycine + 2,3-Butanediol + Water
Find more mixtures with 2,3-Butanediol.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Isopiestic determination of osmotic and activity coefficients of aqueous solutions of aliphatic polyols at 298.15K
- Liquid liquid equilibria of (water + 2,3-butanediol + 2-ethyl-1-hexanol) at several temperatures
- Vapor liquid equilibria for the binary mixtures of 2,3-butanediol with n-butanol, n-butyl acetate, and ethyl acetate at 101.3 kPa
- Liquid liquid equilibria of water + 2,3-butanediol + 1-butanol at T = 298.15 K, T = 308.15K and T = 318.15K
- Liquid liquid equilibria of water + 2,3-butanediol + ethyl acetate at several temperatures
- Osmotic coefficient data and an excess Gibbs energy function for single-phase complex system of glucose + alcohol +water
- Liquid phase behavior of hexafluorophosphate ionic liquids with polyhydric alcohols
- Liquid-liquid equilibria of water + 2,3-butanediol + isobutanol at several temperatures
- Phase behavior of imidazolium and phosphonium tetrafluoroborates with dihydroxy alcohols
- Effect of placement of hydroxyl groups in isomeric butanediol on the behaviour of thermophysical and spectroscopic properties of pyrrolidin-2-one
- A comparative study of thermophysical and spectroscopic properties in mixtures of isomeric butanediol and N,N-dimethylformamide
- Molar heat capacities for (1-butanol + 1,4-butanediol, 2,3-butanediol, 1,2-butanediol, and 2-methyl-2,4-pentanediol) as function of temperature
- (Liquid + liquid) phase equilibria for (water + 2,3-butanediol + oleyl alcohol) at T = (300.2, 307.2, and 314.2) K
- Thermodynamic, transport, and spectroscopic studies for mixtures of isomeric butanediol and N-methyl-2-pyrrolidinone
- Experimental study of the excess molar volume of ternary mixtures containing {water + (1,2-propanediol, or 1,3-propanediol, or 1,2-butanediol, or 1,3-butanediol, or 1,4-butanediol, or 2,3-butanediol) + electrolytes} at a temperature of 298.15 K and atmospheric pressure
- Effect of hydrophilic additives on volumetric and viscosity properties of amino acids in aqueous solutions at T = (283.15 to 333.15) K
- Effect of B-cyclodextrin on the behaviour of thermophysical and spectroscopic properties of binary mixtures of (isomeric butanediol + pyrrolidin-2-one)
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Molar heat capacities for {isomer of butanediol + methanol} as function of mixture composition and temperature
- Enthalpies of dilution of aqueous solutions of n-butanol, butanediols, 1,2,4-butanetriol, and 1,2,3,4-butanetetrol at 298.15K
- Liquid Liquid Equilibria for the Ternary Systems of Water + Butane-2,3-diol + 2-Methylbutan-1-ol, 2-Ethylbutan-1-ol, and 4-Methylpentan-2-ol at 298.15 and 308.15 K
- Densities, Dynamic Viscosities, Speeds of Sound, and Relative Permittivities for Water + Alkanediols (Propane-1,2- and -1,3-diol and Butane-1,2-, -1,3-, -1,4-, and -2,3-Diol) at Different Temperatures
- Densities, partial molar volumes at infinite dilution, side chain partial molar volumes and transfer volumes of dipeptides in sucrose and 2,3- butanediol aqueous solutions at T = (283.15 - 333.15) K
- Solubilities of Carbon Dioxide in Eutectic Mixtures of Choline Chloride and Dihydric Alcohols
- Liquid Liquid Equilibria of Water + 2,3-Butanediol + Butyl Acetate at T ) 298.15 K, T ) 308.15 K, and T ) 318.15 K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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