- InChI
- InChI=1S/C6H12O3/c1-5(4-8-3)9-6(2)7/h5H,4H2,1-3H3
- InChI Key
- LLHKCFNBLRBOGN-UHFFFAOYSA-N
- Formula
- C6H12O3
- SMILES
- COCC(C)OC(C)=O
- Molecular Weight1
- 132.16
- CAS
- 108-65-6
- Other Names
-
- 1-Methoxy-2-propanol acetate
- 1-methoxy-2-acetoxypropane
- 2-(1-Methoxy)propyl acetate
- 2-Methoxy-1-methylethyl acetate
- 2-Propanol, 1-methoxy-, 2-acetate
- 2-acetoxy-1-methoxypropane
- 2-propanol, 1-methoxy-, acetate
- Acetic acid, 2-methoxy-1-methylethyl ester
- Arcosolv PMA
- Dowanol PMA
- Ektasolve PM Acetate
- NSC 2207
- PGMEA
- Propylene glycol 1-methyl ether 2-acetate
- Propyleneglycol monomethyl ether acetate
- propylene glycol 1-monomethyl ether acetate
- Cp,gas : Ideal gas 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).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -341.72 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -549.47 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 11.75 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 40.13 | kJ/mol | Joback Calculated Property |
| log10WS | -0.40 | Crippen Calculated Property | |
| logPoct/wat | 0.584 | Crippen Calculated Property | |
| McVol | 108.710 | ml/mol | McGowan Calculated Property |
| Pc | 3010.00 ± 20.00 | kPa | NIST |
| Inp | [843.00; 914.00] |
|
|
| Inp | 914.00 | NIST | |
| Inp | 857.30 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 843.00 | NIST | |
| I | [1228.00; 1238.30] |
|
|
| I | 1238.30 | NIST | |
| I | 1228.00 | NIST | |
| I | 1228.00 | NIST | |
| Tboil | [418.50; 419.00] | K |
|
| Tboil | 419.00 | K | Isobari... |
| Tboil | 418.65 | K | Solubil... |
| Tboil | 418.50 ± 0.50 | K | NIST |
| Tc | 597.90 ± 1.00 | K | NIST |
| Tfus | 236.77 | K | Joback Calculated Property |
| Vc | 0.407 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [221.96; 277.74] | J/mol×K | [434.95; 616.32] |
|
| Cp,gas | 221.96 | J/mol×K | 434.95 | Joback Calculated Property |
| Cp,gas | 231.96 | J/mol×K | 465.18 | Joback Calculated Property |
| Cp,gas | 241.69 | J/mol×K | 495.41 | Joback Calculated Property |
| Cp,gas | 251.15 | J/mol×K | 525.64 | Joback Calculated Property |
| Cp,gas | 260.32 | J/mol×K | 555.87 | Joback Calculated Property |
| Cp,gas | 269.18 | J/mol×K | 586.09 | Joback Calculated Property |
| Cp,gas | 277.74 | J/mol×K | 616.32 | Joback Calculated Property |
| η | [0.0007770; 0.0010710] | Pa×s | [298.15; 318.15] |
|
| η | 0.0010710 | Pa×s | 298.15 | Densiti... |
| η | 0.0009040 | Pa×s | 308.15 | Densiti... |
| η | 0.0007770 | Pa×s | 318.15 | Densiti... |
| Pvap | [1.62; 101.33] | kPa | [318.27; 418.65] |
|
| Pvap | 1.62 | kPa | 318.27 | Solubil... |
| Pvap | 4.15 | kPa | 335.61 | Solubil... |
| Pvap | 9.25 | kPa | 352.27 | Solubil... |
| Pvap | 13.71 | kPa | 361.27 | Solubil... |
| Pvap | 24.44 | kPa | 375.80 | Solubil... |
| Pvap | 26.70 | kPa | 377.95 | Isobari... |
| Pvap | 40.01 | kPa | 389.25 | Solubil... |
| Pvap | 40.00 | kPa | 389.37 | Isobari... |
| Pvap | 53.30 | kPa | 398.01 | Isobari... |
| Pvap | 66.70 | kPa | 405.04 | Isobari... |
| Pvap | 72.49 | kPa | 407.15 | Solubil... |
| Pvap | 80.00 | kPa | 411.02 | Isobari... |
| Pvap | 93.30 | kPa | 416.25 | Isobari... |
| Pvap | 98.70 | kPa | 418.18 | Isobari... |
| Pvap | 101.33 | kPa | 418.65 | Solubil... |
| ρl | [961.52; 989.20] | kg/m3 | [273.15; 298.15] |
|
| ρl | 989.20 | kg/m3 | 273.15 | Below t... |
| ρl | 978.20 | kg/m3 | 283.15 | Below t... |
| ρl | 961.52 | kg/m3 | 298.15 | Isobari... |
Similar Compounds
![1-[(1-Propoxypropan-2-yl)oxy]propan-2-yl acetate.](data:image/png;base64,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)
Find more compounds similar to 1-Methoxy-2-propyl acetate.
Mixtures
- 1-Methoxy-2-propyl acetate + Water
- 1-Methoxy-2-propyl acetate + 2-Propanol, 1-methoxy-
- 1-Methoxy-2-propyl acetate + Methyl Alcohol
- Carbon dioxide + 1-Methoxy-2-propyl acetate
- Formamide, N,N-dimethyl- + 1-Methoxy-2-propyl acetate
- Benzyl methacrylate + 1-Methoxy-2-propyl acetate
- 1-Methoxy-2-propyl acetate + 2-Propenoic acid, 2-methyl-
- 1-Methoxy-2-propyl acetate + Sulfuryl fluoride
Sources
- Crippen Method
- Crippen Method
- Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
- Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
- Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
- Below the room temperature measurements of CO2 solubilities in six physical absorbents
- Isobaric Vapor Liquid Equilibria for Two Binary Systems {Propylene Glycol Methyl Ether Acetate + Methanol} and {Propylene Glycol Methyl Ether Acetate + N,N-Dimethylformamide} at p = 30.0, 50.0, and 70.0 kPa
- Solubilities of Sulfuryl Fluoride in 2-Butoxyethyl Acetate, 3-Methoxybutyl Acetate, 2-Methoxyethyl Acetate, 1-Methoxy-2-propyl Acetate, and 2-(2-Ethoxyethoxy)ethyl Acetate
- Densities and Viscosities of Binary Mixtures of Propylene Glycol Monomethyl Ether Acetate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate between 298.15 K and 318.15 K
- Solubilities of Three Phosphorus Flame Retardants in Selected Organic Solvents
- 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.