- InChI
- InChI=1S/C4H8O2/c1-2-5-4-6-3-1/h1-4H2
- InChI Key
- VDFVNEFVBPFDSB-UHFFFAOYSA-N
- Formula
- C4H8O2
- SMILES
- C1COCOC1
- Molecular Weight1
- 88.11
- CAS
- 505-22-6
- Other Names
-
- 1,3-dioxacyclohexane
- 1,3-propanediol formal
- m-dioxane
- m-dioxin, dihydro-
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- 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).
- 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).
- IE : Ionization energy (eV).
- 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).
- Inp : Non-polar retention indices.
- 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 |
|---|---|---|---|
| PAff | 825.40 | kJ/mol | NIST |
| BasG | 796.20 | kJ/mol | NIST |
| ΔcH°liquid | [-2340.80; -2322.00] | kJ/mol |
|
| ΔcH°liquid | -2339.86 ± 0.99 | kJ/mol | NIST |
| ΔcH°liquid | -2332.80 ± 1.80 | kJ/mol | NIST |
| ΔcH°liquid | -2331.90 ± 0.84 | kJ/mol | NIST |
| ΔcH°liquid | -2340.80 ± 0.59 | kJ/mol | NIST |
| ΔcH°liquid | -2322.00 | kJ/mol | NIST |
| ΔcH°liquid | -2331.30 ± 0.84 | kJ/mol | NIST |
| ΔfH°gas | [-350.00; -338.40] | kJ/mol |
|
| ΔfH°gas | -338.40 ± 1.10 | kJ/mol | NIST |
| ΔfH°gas | -349.60 | kJ/mol | NIST |
| ΔfH°gas | -350.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | -341.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | [-385.00; -376.60] | kJ/mol |
|
| ΔfH°liquid | -377.50 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -384.60 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | -385.00 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -376.60 ± 0.84 | kJ/mol | NIST |
| ΔfusH° | 12.84 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [35.00; 39.10] | kJ/mol |
|
| ΔvapH° | 39.09 ± 0.05 | kJ/mol | NIST |
| ΔvapH° | 39.10 | kJ/mol | NIST |
| ΔvapH° | 39.10 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.00 | kJ/mol | NIST |
| ΔvapH° | 35.60 | kJ/mol | NIST |
| ΔvapH° | 36.00 ± 0.80 | kJ/mol | NIST |
| IE | [10.10; 10.33] | eV |
|
| IE | 10.33 | eV | NIST |
| IE | 10.12 | eV | NIST |
| IE | 10.12 | eV | NIST |
| IE | 10.10 | eV | NIST |
| log10WS | 0.82 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.381 | Crippen Calculated Property | |
| McVol | 68.100 | ml/mol | McGowan Calculated Property |
| Pc | 5235.81 | kPa | Joback Calculated Property |
| Inp | [701.00; 720.00] |
|
|
| Inp | 701.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 707.00 | NIST | |
| Tboil | 378.70 | K | NIST |
| Tc | 565.69 | K | Relay (1.0) Calculated Property |
| Tfus | 229.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.242 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation, Acentric Factor 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,liquid | 143.90 | J/mol×K | 298.00 | NIST |
| ΔvapH | 39.00 | kJ/mol | 293.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 378.20 | K | 101.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [84.68; 243.15] | 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 | -3.76500e+01 | |||
| Coefficient B | 5.26400e-01 | |||
| Coefficient C | -3.02400e-04 | |||
| Coefficient D | 5.68000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 84.68 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 113.25 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 138.66 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 161.09 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 180.72 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 197.73 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 212.30 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 224.60 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 234.83 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 243.15 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0053315; 0.0003073] | Pa×s | [229.65; 405.15] |
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 | -1.18215e+01 | |||
| Coefficient B | 1.51278e+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. | 229.65 | |||
| Temperature range, max. | 405.15 | |||
| η | 0.0053315 | Pa×s | 229.65 | Calculated Property |
| η | 0.0031838 | Pa×s | 249.15 | Calculated Property |
| η | 0.0020490 | Pa×s | 268.65 | Calculated Property |
| η | 0.0013997 | Pa×s | 288.15 | Calculated Property |
| η | 0.0010035 | Pa×s | 307.65 | Calculated Property |
| η | 0.0007486 | Pa×s | 327.15 | Calculated Property |
| η | 0.0005771 | Pa×s | 346.65 | Calculated Property |
| η | 0.0004574 | Pa×s | 366.15 | Calculated Property |
| η | 0.0003712 | Pa×s | 385.65 | Calculated Property |
| η | 0.0003073 | Pa×s | 405.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [273.93; 403.98] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.52109e+01 | |||
| Coefficient B | -3.82420e+03 | |||
| Coefficient C | -1.76730e+01 | |||
| Temperature range, min. | 273.93 | |||
| Temperature range, max. | 403.98 | |||
| Pvap | 1.33 | kPa | 273.93 | Calculated Property |
| Pvap | 2.96 | kPa | 288.38 | Calculated Property |
| Pvap | 6.05 | kPa | 302.83 | Calculated Property |
| Pvap | 11.55 | kPa | 317.28 | Calculated Property |
| Pvap | 20.78 | kPa | 331.73 | Calculated Property |
| Pvap | 35.51 | kPa | 346.18 | Calculated Property |
| Pvap | 57.99 | kPa | 360.63 | Calculated Property |
| Pvap | 91.02 | kPa | 375.08 | Calculated Property |
| Pvap | 137.94 | kPa | 389.53 | Calculated Property |
| Pvap | 202.66 | kPa | 403.98 | Calculated Property |
Similar Compounds
![Propane, 1,1'-[methylenebis(oxy)]bis[2-methyl-.](data:image/png;base64,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)
![Propane, 1,1'-[ethylidenebis(oxy)]bis-.](data:image/png;base64,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)
Find more compounds similar to 1,3-Dioxane.
Mixtures
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
- Crippen Method
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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