- InChI
- InChI=1S/C6H14O6/c7-1-3(9)5(11)6(12)4(10)2-8/h3-12H,1-2H2/t3-,4+,5+,6-
- InChI Key
- FBPFZTCFMRRESA-GUCUJZIJSA-N
- Formula
- C6H14O6
- SMILES
- OCC(O)C(O)C(O)C(O)CO
- Molecular Weight1
- 182.17
- CAS
- 608-66-2
- Other Names
-
- D-Dulcitol
- Euonymit
- Melampyrin
- Melampyrit
- Melampyrite
- Melampyrum
- NSC 1944
- dulcite
- dulcitol
- dulcose
- 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°solid : Solid 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).
- Tboilr : Boiling point at reduced pressure (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°solid | [-3045.70; -3015.00] | kJ/mol |
|
| ΔcH°solid | -3015.30 | kJ/mol | NIST |
| ΔcH°solid | -3045.70 | kJ/mol | NIST |
| ΔcH°solid | -3015.00 ± 2.00 | kJ/mol | NIST |
| ΔcH°solid | -3015.10 ± 1.80 | kJ/mol | NIST |
| ΔfG° | -831.04 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1101.67 | kJ/mol | Joback Calculated Property |
| ΔfH°solid | [-1347.00; -1346.80] | kJ/mol |
|
| ΔfH°solid | -1347.00 | kJ/mol | NIST |
| ΔfH°solid | -1346.80 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 21.73 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 205.00 | kJ/mol | NIST |
| ΔvapH° | 127.47 | kJ/mol | Joback Calculated Property |
| log10WS | 1.64 | Crippen Calculated Property | |
| logPoct/wat | -3.585 | Crippen Calculated Property | |
| McVol | 130.620 | ml/mol | McGowan Calculated Property |
| Pc | 6830.13 | kPa | Joback Calculated Property |
| S°solid,1 bar | [234.30; 247.70] | J/mol×K |
|
| S°solid,1 bar | 234.30 | J/mol×K | NIST |
| S°solid,1 bar | 247.70 | J/mol×K | NIST |
| Tboil | 888.00 | K | Joback Calculated Property |
| Tc | 1092.90 | K | Joback Calculated Property |
| Tfus | 460.30 ± 0.20 | K | NIST |
| Vc | 0.462 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [423.48; 456.45] | J/mol×K | [888.00; 1092.90] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 425 430 435 440 445 450 455 900 950 1000 1050 | ||||
| Cp,gas | 423.48 | J/mol×K | 888.00 | Joback Calculated Property |
| Cp,gas | 429.90 | J/mol×K | 922.15 | Joback Calculated Property |
| Cp,gas | 435.91 | J/mol×K | 956.30 | Joback Calculated Property |
| Cp,gas | 441.54 | J/mol×K | 990.45 | Joback Calculated Property |
| Cp,gas | 446.82 | J/mol×K | 1024.60 | Joback Calculated Property |
| Cp,gas | 451.78 | J/mol×K | 1058.75 | Joback Calculated Property |
| Cp,gas | 456.45 | J/mol×K | 1092.90 | Joback Calculated Property |
| Cp,solid | 238.50 | J/mol×K | 292.80 | NIST |
| η | [4.5232902e-09; 0.0005812] | Pa×s | [462.30; 888.00] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-4 2.00e-4 3.00e-4 4.00e-4 5.00e-4 6.00e-4 500 600 700 800 | ||||
| η | 0.0005812 | Pa×s | 462.30 | Joback Calculated Property |
| η | 0.0000222 | Pa×s | 533.25 | Joback Calculated Property |
| η | 0.0000018 | Pa×s | 604.20 | Joback Calculated Property |
| η | 0.0000003 | Pa×s | 675.15 | Joback Calculated Property |
| η | 5.1362493e-08 | Pa×s | 746.10 | Joback Calculated Property |
| η | 1.3716255e-08 | Pa×s | 817.05 | Joback Calculated Property |
| η | 4.5232902e-09 | Pa×s | 888.00 | Joback Calculated Property |
| ΔfusH | [65.10; 65.10] | kJ/mol | [460.30; 460.30] |
|
| ΔfusH | 65.10 | kJ/mol | 460.30 | NIST |
| ΔfusH | 65.10 | kJ/mol | 460.30 | NIST |
| ΔfusH | 65.10 | kJ/mol | 460.30 | NIST |
| ΔvapH | 133.80 ± 1.40 | kJ/mol | 480.00 | NIST |
| ΔfusS | 141.40 | J/mol×K | 460.30 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 550.70 | K | 0.10 | NIST |
Similar Compounds
Find more compounds similar to Galactitol.
Mixtures
- Galactitol + Water
- Galactitol + Vitamin C + Water
- Galactitol + Tetraethylammonium bromide + Water
- Galactitol + Water + ammonium bromide
Sources
- Crippen Method
- Crippen Method
- 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
- Investigations to explore interactions in (polyhydroxy solute + L-ascorbic acid + H2O) solutions at different temperatures: Calorimetric and viscometric approach
- Densities and Viscosities of Polyhydroxy Solutes in Aqueous Tetraethylammonium Bromide Solutions at Different Temperatures
- Influence of NH4Br on Solvation Behavior of Polyhydroxy Solutes in Aqueous Solutions at Different Temperatures and Atmospheric Pressure
- Joback 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.