- InChI
- InChI=1S/C4H10O4/c5-1-3(7)4(8)2-6/h3-8H,1-2H2/t3-,4+
- InChI Key
- UNXHWFMMPAWVPI-ZXZARUISSA-N
- Formula
- C4H10O4
- SMILES
- OCC(O)C(O)CO
- Molecular Weight1
- 122.12
- CAS
- 149-32-6
- Other Names
-
- (R*,S*)-1,2,3,4-butanetetrol
- 1,2,3,4-Butanetetrol, (2R,3S)-rel-
- 1,2,3,4-Butanetetrol, (R*,S*)-
- 1,2,3,4-Tetrahydroxybutane, (R*,S*)-
- 2(R),3(S)-1,2,3,4-Butanetetrol
- Antierythrite
- C*Eridex
- Erythrit
- Erythrite
- Erythritol, meso-
- Erythroglucin
- Erythrol
- L-Erythritol
- Lichen sugar
- NIK 242
- NSC 8099
- Paycite
- Phycitol
- TETRAHYDOXYBUTANE
- meso-1,2,3,4-butanetetrol
- meso-Erythritol
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid 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).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation 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).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- 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 | -2092.80 ± 1.30 | kJ/mol | NIST |
| ΔcH°solid | -2118.00 | kJ/mol | NIST |
| ΔfG° | -569.36 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -745.37 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -910.48 ± 0.54 | kJ/mol | NIST |
| ΔfusH° | 39.93 | kJ/mol | Measure... |
| ΔsubH° | [135.00; 157.00] | kJ/mol |
|
| ΔsubH° | 140.00 | kJ/mol | NIST |
| ΔsubH° | 157.00 | kJ/mol | NIST |
| ΔsubH° | 135.00 | kJ/mol | NIST |
| ΔvapH° | 93.30 | kJ/mol | NIST |
| log10WS | [0.70; 0.70] |
|
|
| log10WS | 0.70 | Aq. Sol... | |
| log10WS | 0.70 | Estimat... | |
| logPoct/wat | -2.307 | Crippen Calculated Property | |
| McVol | 90.700 | ml/mol | McGowan Calculated Property |
| Pc | 6740.71 | kPa | Joback Calculated Property |
| S°solid,1 bar | [166.50; 177.80] | J/mol×K |
|
| S°solid,1 bar | 166.50 | J/mol×K | NIST |
| S°solid,1 bar | 177.80 | J/mol×K | NIST |
| Tboil | 603.70 | K | NIST |
| Tc | 819.90 | K | Joback Calculated Property |
| Tfus | [390.50; 394.90] | K |
|
| Tfus | 394.90 | K | Aq. Sol... |
| Tfus | 392.05 | K | KDB |
| Tfus | 390.50 | K | Solid-l... |
| Tfus | 394.82 | K | Heat ca... |
| Tfus | 390.90 ± 0.20 | K | NIST |
| Tfus | 391.60 ± 0.20 | K | NIST |
| Vc | 0.324 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [248.93; 277.70] | J/mol×K | [658.76; 819.90] |
|
| Cp,gas | 248.93 | J/mol×K | 658.76 | Joback Calculated Property |
| Cp,gas | 254.30 | J/mol×K | 685.62 | Joback Calculated Property |
| Cp,gas | 259.43 | J/mol×K | 712.47 | Joback Calculated Property |
| Cp,gas | 264.33 | J/mol×K | 739.33 | Joback Calculated Property |
| Cp,gas | 269.00 | J/mol×K | 766.19 | Joback Calculated Property |
| Cp,gas | 273.46 | J/mol×K | 793.04 | Joback Calculated Property |
| Cp,gas | 277.70 | J/mol×K | 819.90 | Joback Calculated Property |
| Cp,solid | [161.90; 170.70] | J/mol×K | [291.70; 303.00] |
|
| Cp,solid | 161.90 | J/mol×K | 291.70 | NIST |
| Cp,solid | 170.70 | J/mol×K | 303.00 | NIST |
| η | [0.0000022; 0.0672433] | Pa×s | [348.12; 658.76] |
|
| η | 0.0672433 | Pa×s | 348.12 | Joback Calculated Property |
| η | 0.0039218 | Pa×s | 399.89 | Joback Calculated Property |
| η | 0.0004388 | Pa×s | 451.67 | Joback Calculated Property |
| η | 0.0000770 | Pa×s | 503.44 | Joback Calculated Property |
| η | 0.0000187 | Pa×s | 555.21 | Joback Calculated Property |
| η | 0.0000058 | Pa×s | 606.99 | Joback Calculated Property |
| η | 0.0000022 | Pa×s | 658.76 | Joback Calculated Property |
| ΔfusH | [38.90; 42.36] | kJ/mol | [381.60; 396.00] |
|
| ΔfusH | 42.36 | kJ/mol | 381.60 | NIST |
| ΔfusH | 39.40 | kJ/mol | 390.90 | NIST |
| ΔfusH | 38.90 | kJ/mol | 391.20 | NIST |
| ΔfusH | 40.30 | kJ/mol | 392.20 | NIST |
| ΔfusH | 42.36 | kJ/mol | 396.00 | NIST |
| ΔvapH | [93.30; 113.60] | kJ/mol | [397.50; 412.50] |
|
| ΔvapH | 93.30 | kJ/mol | 397.50 | NIST |
| ΔvapH | 97.00 ± 1.00 | kJ/mol | 398.00 | NIST |
| ΔvapH | 113.60 ± 1.10 | kJ/mol | 412.50 | NIST |
| ΔfusS | [100.80; 111.00] | J/mol×K | [381.60; 390.90] |
|
| ΔfusS | 111.00 | J/mol×K | 381.60 | NIST |
| ΔfusS | 100.80 | J/mol×K | 390.90 | NIST |
Similar Compounds
![1,2,3,4-Butanetetrol, [S-(R*,R*)]-.](data:image/png;base64,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)
Find more compounds similar to Erythritol.
Mixtures
- Vitamin C + Erythritol + Water
- Erythritol + Water
- Ethanol + Erythritol + Methyl Alcohol
- Ethanol + Erythritol
- Erythritol + Methyl Alcohol
- Acetone + Erythritol
- Ethanol + Erythritol + Water
- Erythritol + Methyl Alcohol + Water
- Erythritol + Tetrahydrofuran + Water
Sources
- Crippen Method
- Isopiestic determination of osmotic and activity coefficients of aqueous solutions of aliphatic polyols at 298.15K
- Solubility of erythritol in methanol, ethanol and methanol + ethanol: Experimental measurement and thermodynamic modeling
- Solid-liquid phase equilibria in binary mixtures of functionalized ionic liquids with sugar alcohols: New experimental data and modelling
- Partitioning of diuron in a novel aqueous two-phase system based on polyols and tetrahydrofuran
- Apparent molar volumes and apparent molar heat capacities of aqueous adonitol, dulcitol, glycerol, meso-erythritol, myo-inositol, D-sorbitol, and xylitol at temperatures from (278.15 to 368.15) K and at the pressure 0.35 MPa
- Heat capacities of some sugar alcohols as phase change materials for thermal energy storage applications
- Enthalpies of dilution of aqueous solutions of n-butanol, butanediols, 1,2,4-butanetriol, and 1,2,3,4-butanetetrol at 298.15K
- Measurement of enthalpy curves of phase change materials via DSC and T-History: When are both methods needed to estimate the behaviour of the bulk material in applications?
- Densities and Viscosities of Sugar Alcohols in Vitamin B6 Aqueous Solutions at (293.15 to 323.15) K
- Solubility of Erythritol in Different Solvents
- Densities and Viscosities of Erythritol, Xylitol, and Mannitol in l-ascorbic Acid Aqueous Solutions at T = (293.15 to 323.15) K
- Densities and Viscosities of Sugar Alcohol Aqueous Solutions
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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.