- InChI
- InChI=1S/C6H14O6/c7-1-3(9)5(11)6(12)4(10)2-8/h3-12H,1-2H2/t3-,4-,5-,6-/m1/s1
- InChI Key
- FBPFZTCFMRRESA-KVTDHHQDSA-N
- Formula
- C6H14O6
- SMILES
-
OC[C@H](O)[C@H](O)[C@@H](O)[C@
@H](O)CO - Molecular Weight1
- 182.17
- CAS
- 69-65-8
- Other Names
-
- 1,2,3,4,5,6-Hexanehexol
- Cordycepic acid
- D-(-)-mannitol
- Diosmol
- Isotol
- Manicol
- Maniton-S
- Manna sugar
- Mannazucker
- Mannazucker (German)
- Mannidex
- Mannigen
- Mannistol
- Mannit
- Mannite
- Mannitol
- Mannitol, D-
- Mannogem 2080
- Marine Crystal
- NCI-C50362
- Osmitrol
- Osmosal
- Partek M
- Pearlitol 25C
- Resectisol
- 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).
- 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 | [-3053.00; -3024.70] | kJ/mol |
|
| ΔcH°solid | -3053.00 | kJ/mol | NIST |
| ΔcH°solid | -3045.70 | kJ/mol | NIST |
| ΔcH°solid | -3025.00 ± 2.00 | kJ/mol | NIST |
| ΔcH°solid | -3024.70 ± 1.80 | kJ/mol | NIST |
| ΔfH°gas | -1019.23 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | [-1337.50; -1337.20] | kJ/mol |
|
| ΔfH°solid | -1337.50 | kJ/mol | NIST |
| ΔfH°solid | -1337.20 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 54.69 | kJ/mol | Heat Capacities and Nonisothermal Thermal Decomposition Reaction Kinetics of d-Mannitol |
| ΔsubH° | 202.00 | kJ/mol | NIST |
| ΔvapH° | 112.41 | kJ/mol | Relay (1.0) Calculated Property |
| log10WS | 0.06 | Estimated Solubility | |
| 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 | [238.50; 253.10] | J/mol×K |
|
| S°solid,1 bar | 238.50 | J/mol×K | NIST |
| S°solid,1 bar | 253.10 | J/mol×K | NIST |
| Tboil | 678.50 | K | Relay (1.0) Calculated Property |
| Tc | 956.29 | K | Relay (1.0) Calculated Property |
| Tfus | [435.00; 440.65] | K |
|
| Tfus | 440.62 | K | Heat capacities of some sugar alcohols as phase change materials for thermal energy storage applications |
| Tfus | Outlier 435.00 | K | Nanocalorimetry measurements of metastable states |
| Tfus | 438.88 | K | Cycling stability of D-mannitol when used as phase change material for thermal storage applications |
| Tfus | 440.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 439.13 | K | KDB |
| Tfus | 439.10 ± 0.10 | K | NIST |
| Tfus | 439.00 ± 1.00 | K | NIST |
| Tfus | 439.20 ± 0.20 | K | NIST |
| Tfus | 439.13 ± 0.20 | K | NIST |
| Tfus | 439.20 ± 0.20 | K | NIST |
| Vc | 0.511 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation, Acentric Factor, Ionization energy for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | [236.00; 244.80] | J/mol×K | [294.10; 303.00] |
|
| Cp,solid | 236.00 | J/mol×K | 294.10 | NIST |
| Cp,solid | 239.00 | J/mol×K | 298.15 | NIST |
| Cp,solid | 244.80 | J/mol×K | 303.00 | NIST |
| ΔfusH | [53.58; 56.10] | kJ/mol | [433.20; 439.10] |
|
| ΔfusH | 53.58 | kJ/mol | 433.20 | NIST |
| ΔfusH | 53.58 | kJ/mol | 433.20 | NIST |
| ΔfusH | 54.69 | kJ/mol | 437.30 | NIST |
| ΔfusH | 56.10 | kJ/mol | 439.10 | NIST |
| ΔfusH | 56.10 | kJ/mol | 439.10 | NIST |
| ΔvapH | 135.60 ± 1.10 | kJ/mol | 479.50 | NIST |
| ΔfusS | [123.70; 127.80] | J/mol×K | [433.20; 439.10] |
|
| ΔfusS | 123.70 | J/mol×K | 433.20 | NIST |
| ΔfusS | 123.70 | J/mol×K | 433.20 | NIST |
| ΔfusS | 127.80 | J/mol×K | 439.10 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 568.20 | K | 0.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [206.51; 443.05] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.24520e+01 | |||
| Coefficient B | 8.01400e-01 | |||
| Coefficient C | -4.97800e-04 | |||
| Coefficient D | 1.17000e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 206.51 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 248.85 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 286.30 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 319.25 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 348.07 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 373.12 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 394.77 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 413.40 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 429.37 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 443.05 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0020838; 3.5139340e-08] | Pa×s | [439.43; 765.20] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -3.19890e+01 | |||
| Coefficient B | 1.13442e+04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 439.43 | |||
| Temperature range, max. | 765.20 | |||
| η | 0.0020838 | Pa×s | 439.43 | Calculated Property |
| η | 0.0002922 | Pa×s | 475.63 | Calculated Property |
| η | 0.0000541 | Pa×s | 511.83 | Calculated Property |
| η | 0.0000125 | Pa×s | 548.02 | Calculated Property |
| η | 0.0000035 | Pa×s | 584.22 | Calculated Property |
| η | 0.0000011 | Pa×s | 620.42 | Calculated Property |
| η | 0.0000004 | Pa×s | 656.61 | Calculated Property |
| η | 0.0000002 | Pa×s | 692.81 | Calculated Property |
| η | 7.3362681e-08 | Pa×s | 729.01 | Calculated Property |
| η | 3.5139340e-08 | Pa×s | 765.20 | Calculated Property |
Similar Compounds
Find more compounds similar to D-Mannitol.
Mixtures
- D-Mannitol + Dimethyl Sulfoxide
- D-Mannitol + Glycine + Water
- D-Mannitol + Water
- D-Alanine + D-Mannitol + Water
- D-Mannitol + D-Valine + Water
- Threonine + D-Mannitol + Water
- D-Mannitol + (-)-D-arginine hydrate + Water
- 1-Propanol + D-Mannitol + Water
- 2-Propanol + D-Mannitol + Water
- D-Mannitol + Ethanol + Water
- D-Mannitol + Ethanol
- D-Mannitol + Vitamin C + Water
- D-Mannitol + Water + Cetrimonium Bromide
- D-Mannitol + Water + Ammonium bromide
- D-Mannitol + Water + Rofecoxib
- Sorbitol + D-Mannitol + Water
- Sucrose + D-Mannitol + Water
- D-Mannitol + Water + N,N'-DIACETYLHEXAMETHYLENEDIAMINE
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Modulation in physico-chemical characteristics of some polyhydroxy solutes in presence of L-glycine: Volumetric and NMR spectroscopic approach
- Rheological and time domain 1H NMR relaxation studies of some polyhydroxy solutes in presence of L-glycine
- Heat capacities of some sugar alcohols as phase change materials for thermal energy storage applications
- Nanocalorimetry measurements of metastable states
- Dielectric relaxation and thermodynamic study of polyhydric sugar alcohols in DMSO using TDR technique
- Cycling stability of D-mannitol when used as phase change material for thermal storage applications
- Solubility of Rofecoxib in the Presence of Mannitol, Poly(vinylpyrrolidone) K30, Urea, Polyethylene Glycol 4000, and Polyethylene Glycol 6000 at (298.15, 303.15, and 308.15) K
- Viscosity and Density of the Nonelectrolyte System Mannitol + Sorbitol + Sucrose + H2O and Its Binary and Ternary Subsystems at 298.15 K
- Apparent Molar Volumes and Viscosity B-Coefficients of Carbohydrates in Aqueous Cetrimonium Bromide Solutions at (298.15, 308.15, and 318.15) K
- Enthalpies of Dilution, Volumetric Properties, and Refractive Indices of N,N'-Hexamethylenebisacetamide in Aqueous Xylitol or d-Mannitol Solutions at T = 298.15 K
- Ionic Liquids as Promising Solvents for Biomass Derived Mannitol and Xylitol
- Densities and Viscosities of Erythritol, Xylitol, and Mannitol in l-ascorbic Acid Aqueous Solutions at T = (293.15 to 323.15) K
- Influence of NH4Br on Solvation Behavior of Polyhydroxy Solutes in Aqueous Solutions at Different Temperatures and Atmospheric Pressure
- Volumetric and Viscometric Studies of Amino Acids in Mannitol Aqueous Solutions at T = (293.15 to 323.15) K
- Properties of Sugar, Polyol, and Polysaccharide Water-Ethanol Solutions
- Transfer Enthalpies of Amino Acids and Glycine Peptides from Water to Aqueous Solutions of Sugar Alcohol at 298.15 K
- Heat Capacities and Nonisothermal Thermal Decomposition Reaction Kinetics of d-Mannitol
- Molar Volumes and Refractive Indexes of Hexane-1,2,3,4,5,6-hexol in Aqueous Solutions of 1-Propanol and 2-Propanol
- Densities and Viscosities of Sugar Alcohol Aqueous Solutions
- Joback Method
- KDB
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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