- InChI
- InChI=1S/C3H6O2/c1-2-5-3-4-1/h1-3H2
- InChI Key
- WNXJIVFYUVYPPR-UHFFFAOYSA-N
- Formula
- C3H6O2
- SMILES
- C1COCO1
- Molecular Weight1
- 74.08
- CAS
- 646-06-0
- Other Names
-
- 1,3-Dioxacyclopentane
- 1,3-Dioxolan
- 1,3-Dioxole, dihydro-
- Dioxolan
- Dioxolane
- Ethylene glycol formal
- Formal glycol
- Glycolformal
- dihydro-1,3-dioxole
- ethylene glycol methylene ether
- formaldehyde ethylene acetal
- 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).
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 | [-1705.00; -1700.00] | kJ/mol |
|
| ΔcH°liquid | -1700.80 ± 1.40 | kJ/mol | NIST |
| ΔcH°liquid | -1700.00 | kJ/mol | NIST |
| ΔcH°liquid | -1705.00 | kJ/mol | NIST |
| η | 0.0005310 | Pa×s | Excess ... |
| ΔfG° | -153.60 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -301.70 ± 2.20 | kJ/mol | NIST |
| ΔfH°liquid | -337.20 ± 1.40 | kJ/mol | NIST |
| ΔfusH° | 12.35 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [35.50; 36.00] | kJ/mol |
|
| ΔvapH° | 35.50 | kJ/mol | NIST |
| ΔvapH° | 36.00 ± 0.40 | kJ/mol | NIST |
| IE | [9.90; 10.10] | eV |
|
| IE | 9.90 | eV | NIST |
| IE | 10.02 | eV | NIST |
| IE | 10.10 | eV | NIST |
| log10WS | 0.36 | Crippen Calculated Property | |
| logPoct/wat | -0.009 | Crippen Calculated Property | |
| McVol | 54.010 | ml/mol | McGowan Calculated Property |
| Pc | 5818.28 | kPa | Joback Calculated Property |
| Inp | [582.00; 638.00] |
|
|
| Inp | 638.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 635.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 635.00 | NIST | |
| I | 935.00 | NIST | |
| S°gas | 310.50 ± 4.10 | J/mol×K | NIST |
| S°liquid | 280.20 | J/mol×K | NIST |
| Tboil | [339.12; 348.75] | K |
|
| Tboil | 339.12 | K | Study o... |
| Tboil | 348.57 | K | Vapor-L... |
| Tboil | 348.00 | K | Study o... |
| Tboil | 347.70 | K | NIST |
| Tboil | 348.75 | K | NIST |
| Tc | 543.20 | K | Joback Calculated Property |
| Tfus | [175.85; 175.90] | K |
|
| Tfus | 175.85 | K | NIST |
| Tfus | 175.90 ± 0.60 | K | NIST |
| Ttriple | 175.93 ± 0.02 | K | NIST |
| Vc | 0.188 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [87.73; 133.05] | J/mol×K | [341.89; 543.20] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 90 100 110 120 130 350 400 450 500 | ||||
| Cp,gas | 87.73 | J/mol×K | 341.89 | Joback Calculated Property |
| Cp,gas | 96.41 | J/mol×K | 375.44 | Joback Calculated Property |
| Cp,gas | 104.62 | J/mol×K | 408.99 | Joback Calculated Property |
| Cp,gas | 112.37 | J/mol×K | 442.54 | Joback Calculated Property |
| Cp,gas | 119.68 | J/mol×K | 476.09 | Joback Calculated Property |
| Cp,gas | 126.57 | J/mol×K | 509.65 | Joback Calculated Property |
| Cp,gas | 133.05 | J/mol×K | 543.20 | Joback Calculated Property |
| Cp,liquid | [118.00; 129.50] | J/mol×K | [288.15; 328.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 118 120 122 124 126 128 130 290 300 310 320 | ||||
| Cp,liquid | 118.80 | J/mol×K | 288.15 | Thermop... |
| Cp,liquid | 120.30 | J/mol×K | 293.15 | Thermop... |
| Cp,liquid | 118.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 121.70 | J/mol×K | 298.15 | Thermop... |
| Cp,liquid | 120.84 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 123.30 | J/mol×K | 303.15 | Thermop... |
| Cp,liquid | 124.40 | J/mol×K | 308.15 | Thermop... |
| Cp,liquid | 125.30 | J/mol×K | 313.15 | Thermop... |
| Cp,liquid | 126.80 | J/mol×K | 318.15 | Thermop... |
| Cp,liquid | 128.10 | J/mol×K | 323.15 | Thermop... |
| Cp,liquid | 129.50 | J/mol×K | 328.15 | Thermop... |
| η | [0.0004580; 0.0005878] | Pa×s | [298.15; 318.15] |
|
| η | 0.0005878 | Pa×s | 298.15 | Studies... |
| η | 0.0005128 | Pa×s | 308.15 | Studies... |
| η | 0.0004580 | Pa×s | 318.15 | Studies... |
| ΔfusH | [2.68; 6.57] | kJ/mol | [142.40; 175.90] |
|
| ΔfusH | 2.68 | kJ/mol | 142.40 | NIST |
| ΔfusH | 6.57 | kJ/mol | 175.90 | NIST |
| ΔfusH | 6.57 | kJ/mol | 175.90 | NIST |
| ΔvapH | [33.70; 35.80] | kJ/mol | [301.50; 339.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 33.5 34 34.5 35 35.5 36 310 320 330 | ||||
| ΔvapH | 35.80 | kJ/mol | 301.50 | NIST |
| ΔvapH | 34.10 | kJ/mol | 317.50 | NIST |
| ΔvapH | 34.60 | kJ/mol | 326.00 | NIST |
| ΔvapH | 33.70 | kJ/mol | 326.00 | NIST |
| ΔvapH | 33.70 | kJ/mol | 339.00 | NIST |
| ν | [0.0000005; 0.0000007] | m2/s | [283.15; 313.15] |
|
| ν | 0.0000007 | m2/s | 283.15 | Experim... |
| ν | 0.0000006 | m2/s | 298.15 | Experim... |
| ν | 0.0000005 | m2/s | 313.15 | Experim... |
| Pvap | [5.42; 49.01] | kPa | [280.46; 328.15] |
|
|
T(K) Vapor pressure (kPa) 10 20 30 40 50 280 300 320 | ||||
| Pvap | 5.42 | kPa | 280.46 | Vapor P... |
| Pvap | 6.20 | kPa | 282.96 | Vapor P... |
| Pvap | 7.14 | kPa | 285.51 | Vapor P... |
| Pvap | 7.91 | kPa | 287.44 | Vapor P... |
| Pvap | 10.78 | kPa | 293.48 | Vapor P... |
| Pvap | 13.59 | kPa | 298.12 | Vapor P... |
| Pvap | 13.54 | kPa | 298.15 | Isother... |
| Pvap | 13.54 | kPa | 298.15 | Isother... |
| Pvap | 15.69 | kPa | 301.25 | Vapor P... |
| Pvap | 17.05 | kPa | 303.00 | Vapor P... |
| Pvap | 19.15 | kPa | 305.57 | Vapor P... |
| Pvap | 23.08 | kPa | 309.76 | Vapor P... |
| Pvap | 26.83 | kPa | 313.15 | Isother... |
| Pvap | 26.73 | kPa | 313.16 | Vapor P... |
| Pvap | 31.18 | kPa | 316.81 | Vapor P... |
| Pvap | 49.01 | kPa | 328.15 | Isother... |
| Pvap | 49.01 | kPa | 328.15 | Isother... |
| n0 | [1.39740; 1.39800] | [298.15; 298.15] |
|
|
| n0 | 1.39800 | 298.15 | Studies... | |
| n0 | 1.39740 | 298.15 | Physics... | |
| n0 | 1.39779 | 298.15 | Vapor-L... | |
| ρl | [1046.30; 1059.00] | kg/m3 | [298.15; 308.15] |
|
|
T(K) Liquid Density (kg/m3) 1046 1048 1050 1052 1054 1056 1058 1060 300 305 | ||||
| ρl | 1047.20 | kg/m3 | 298.15 | Thermod... |
| ρl | 1059.00 | kg/m3 | 298.15 | Vapour ... |
| ρl | 1058.73 | kg/m3 | 298.15 | Ionic s... |
| ρl | 1058.62 | kg/m3 | 298.15 | (Vapour... |
| ρl | 1058.62 | kg/m3 | 298.15 | Surface... |
| ρl | 1058.70 | kg/m3 | 298.15 | Probing... |
| ρl | 1058.76 | kg/m3 | 298.15 | Isother... |
| ρl | 1058.62 | kg/m3 | 298.15 | Experim... |
| ρl | 1058.90 | kg/m3 | 298.15 | Densiti... |
| ρl | 1051.80 | kg/m3 | 303.15 | Viscous... |
| ρl | 1052.60 | kg/m3 | 303.15 | Densiti... |
| ρl | 1046.30 | kg/m3 | 308.15 | Densiti... |
| ΔfusS | [18.80; 37.33] | J/mol×K | [142.40; 175.90] |
|
| ΔfusS | 18.80 | J/mol×K | 142.40 | NIST |
| ΔfusS | 37.33 | J/mol×K | 175.90 | NIST |
| csound,fluid | [1270.90; 1406.30] | m/s | [283.15; 313.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1260 1280 1300 1320 1340 1360 1380 1400 290 300 310 | ||||
| csound,fluid | 1406.30 | m/s | 283.15 | Speeds ... |
| csound,fluid | 1339.90 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1340.20 | m/s | 298.15 | Densiti... |
| csound,fluid | 1271.60 | m/s | 313.15 | Speeds ... |
| csound,fluid | 1270.90 | m/s | 313.15 | Densiti... |
| γ | [0.03; 0.03] | N/m | [288.15; 308.15] |
|
| γ | 0.03 | N/m | 288.15 | Densiti... |
| γ | 0.03 | N/m | 298.15 | Densiti... |
| γ | 0.03 | N/m | 308.15 | Densiti... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 214.40] | kPa | [256.45; 372.15] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.46333e+01 | |||
| Coefficient B | -3.02711e+03 | |||
| Coefficient C | -4.54420e+01 | |||
| Temperature range, min. | 256.45 | |||
| Temperature range, max. | 372.15 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 256.45 | Calculated Property |
| Pvap | 3.04 | kPa | 269.31 | Calculated Property |
| Pvap | 6.33 | kPa | 282.16 | Calculated Property |
| Pvap | 12.23 | kPa | 295.02 | Calculated Property |
| Pvap | 22.16 | kPa | 307.87 | Calculated Property |
| Pvap | 37.98 | kPa | 320.73 | Calculated Property |
| Pvap | 62.03 | kPa | 333.58 | Calculated Property |
| Pvap | 97.16 | kPa | 346.44 | Calculated Property |
| Pvap | 146.69 | kPa | 359.29 | Calculated Property |
| Pvap | 214.40 | kPa | 372.15 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,3-Dioxolane.
Mixtures
- 1,3-Dioxolane + Cyclopentane
- 1,3-Dioxolane + Cyclohexane
- 1,3-Dioxolane + Benzene
- 1,3-Dioxolane + Methyl Alcohol + Water
- 1,3-Dioxolane + Ethanol + Water
- 1,3-Dioxolane + 1-Propanol + Water
- 1,3-Dioxolane + Isopropyl Alcohol + Water
- 1,3-Dioxolane + 1-Butanol + Water
- 2-Propanol, 2-methyl- + 1,3-Dioxolane + Water
- 1,3-Dioxolane + 1-Butanol, 3-methyl- + Water
- 1,3-Dioxolane + Pentane, 1-chloro-
- 1,3-Dioxolane + Hexane, 1-chloro-
- 1,3-Dioxolane + n-Propyl chloride
- 1,3-Dioxolane + Tetrabutylammonium hexafluorophosphate
- 1,3-Dioxolane + 1-Propanol, 2-methyl-
- 2-Propanol, 2-methyl- + 1,3-Dioxolane
- 1,3-Dioxolane + Butane, 1-chloro-
- 1,3-Dioxolane + Butane, 2-chloro-
- 1,3-Dioxolane + Propane, 1-chloro-2-methyl-
- 1,3-Dioxolane + Propane, 2-chloro-2-methyl-
Find more mixtures with 1,3-Dioxolane.
Sources
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
- Partial Molar Volumes, Viscosity B-Coefficients, and Adiabatic Compressibilities of Sodium Molybdate in Aqueous 1,3-Dioxolane Mixtures from 303.15 to 323.15 K
- Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
- Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
- Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
- Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
- Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
- Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
- Separation of 1,3-dioxolane from its azeotropic aqueous solution by using Good's buffer ionic liquid [TMA][EPPS]
- (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
- Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
- Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
- Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
- Partial molar volumes of organic solutes in water. XXII. Cyclic ethers at temperatures (298 to 573) K and pressures up to 30 MPa
- Probing subsistence of ion-pair and triple-ion of an ionic salt in liquid environments by means of conductometric contrivance
- (Liquid + liquid), (solid + liquid), and (solid + liquid + liquid) equilibria of systems containing cyclic ether (tetrahydrofuran or 1,3-dioxolane), water, and a biological buffer MOPS
- Excess molar volumes and excess isentropic compressibilities of mixtures containing lactam, cyclic ethers and cyclic alkanones
- Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
- Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
- Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
- Thermodynamic properties of liquid mixtures containing 1,3-dioxolane and anilines: Excess molar volumes, excess molar enthalpies, excess Gibb's free energy and isentropic compressibilities changes of mixing
- Physics and Chemistry of Lithium Halides in 1,3-Dioxolane and Its Binary Mixtures with Acetonitrile probed by Conductometric, Volumetric, Viscometric, Refractometric and Acoustic Study
- Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
- Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
- Vapor-Liquid Equilibrium Data for Methanol + 1,3-Dioxolane + Water and Constituent Binary Systems at 101.3 kPa.
- Experimental and predicted viscosities of the ternary mixture (hexane + 1,3-dioxolane + 2-butanol) at 298.15 and 313.15 K
- Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
- Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
- Isobaric Vapor Liquid Equilibrium for the Ternary System (Formaldehyde + 1,3-Dioxolane + Water) at 101.3 kPa
- Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
- Studies on Molecular Interactions of Some Thiocyanate Salts in Coaqueous Solutions of 1,3-Dioxolane + Water by Volumetric, Viscometric, and Speed of Sound Measurements
- Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
- Density, Viscosity, Refractive Index, and Ultrasonic Speed of Binary Mixtures of 1,3-Dioxolane with 2-Methoxyethanol, 2-Ethoxyethanol, 2-Butoxyethanol, 2-Propylamine, and Cyclohexylamine
- Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
- Study of Solution Properties of Some Alkali Bromides in Aqueous Binary Mixtures of 1,3-Dioxolane in View of Different Models
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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