- InChI
- InChI=1S/C5H10O5/c6-1-3(8)5(10)4(9)2-7/h1,3-5,7-10H,2H2/t3-,4-,5+/m0/s1
- InChI Key
- PYMYPHUHKUWMLA-VAYJURFESA-N
- Formula
- C5H10O5
- SMILES
-
O=C[C@H](O)[C@@H](O)[C@@H](O)C
O - Molecular Weight1
- 150.13
- CAS
- 87-72-9
- Other Names
-
- (+)-arabinose
- (3R,4S,5S)-tetrahydro-2H-pyran-2,3,4,5-tetraol
- Arabinose(L)
- L-(+)-arabinose
- L-arabinopyranose
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Tboil : Normal Boiling Point Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfusH° | 16.78 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 88.18 | kJ/mol | Relay (1.0) Calculated Property |
| log10WS | [0.39; 0.39] |
|
|
| log10WS | 0.39 | Aq. Solubility Prediction | |
| log10WS | 0.39 | Estimated Solubility | |
| logPoct/wat | -2.740 | Crippen Calculated Property | |
| McVol | 106.360 | ml/mol | McGowan Calculated Property |
| Tboil | 602.25 | K | Relay (1.0) Calculated Property |
| Tfus | 431.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of formation at standard conditions, 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 | 184.00 | J/mol×K | 303.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [165.52; 344.36] | 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 | 2.58610e+01 | |||
| Coefficient B | 6.07000e-01 | |||
| Coefficient C | -3.72400e-04 | |||
| Coefficient D | 8.39000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 165.52 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 197.71 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 226.20 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 251.25 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 273.14 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 292.13 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 308.48 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 322.46 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 334.33 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 344.36 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0018473; 0.0000054] | Pa×s | [431.15; 630.61] |
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 | -2.47695e+01 | |||
| Coefficient B | 7.96569e+03 | |||
| 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. | 431.15 | |||
| Temperature range, max. | 630.61 | |||
| η | 0.0018473 | Pa×s | 431.15 | Calculated Property |
| η | 0.0007486 | Pa×s | 453.31 | Calculated Property |
| η | 0.0003300 | Pa×s | 475.47 | Calculated Property |
| η | 0.0001565 | Pa×s | 497.64 | Calculated Property |
| η | 0.0000791 | Pa×s | 519.80 | Calculated Property |
| η | 0.0000423 | Pa×s | 541.96 | Calculated Property |
| η | 0.0000237 | Pa×s | 564.12 | Calculated Property |
| η | 0.0000139 | Pa×s | 586.29 | Calculated Property |
| η | 0.0000085 | Pa×s | 608.45 | Calculated Property |
| η | 0.0000054 | Pa×s | 630.61 | Calculated Property |
Similar Compounds
Find more compounds similar to L-Arabinose.
Mixtures
- Water + L-Arabinose
- Tetrahydrofuran + Water + L-Arabinose
- (-)-D-arginine hydrate + Water + L-Arabinose
- Water + 1,4,7,10,13,16-Hexaoxacyclooctadecane + L-Arabinose
- xylose + Water + L-Arabinose
- L-Phenylalanine + Water + L-Arabinose
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)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Osmotic properties of carbohydrate aqueous solutions
- Novel phase diagrams of aqueous two-phase systems based on tetrahydrofuran + carbohydrates + water: equilibrium data and partitioning experiments
- A quasi-ternary wet residue method applied to solid-liquid equilibrium systems
- Evaluation of the effect of ionic-liquids as soluting-out agents on the solubility of carbohydrates in aqueous solutions
- Probing solute solute and solute solvent interactions in (l-arginine + d-xylose/ l-arabinose + water) solutions at different temperatures by using volumetric and viscometric methods
- Physicochemical study of solute-solute and solute-solvent interactions of l-phenylalanine in (water + arabinose/glucose/sucrose) solutions at different temperatures
- Soluting-out effect of carbohydrates on the surface active ionic liquid 1-decyl-3-methylimidazolium bromide in aqueous solutions
- Thermochemical behavior of 18-crown-6 in aqueous solutions of some monosaccharides
- Extractions of Alkaloids Codeine and Caffeine with [Bmim][BF4]/Carbohydrate Aqueous Biphasic Systems as a Novel Class of Liquid-Liquid Extraction Systems
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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