- InChI
- InChI=1S/C4H10O2/c1-4(5)3-6-2/h4-5H,3H2,1-2H3
- InChI Key
- ARXJGSRGQADJSQ-UHFFFAOYSA-N
- Formula
- C4H10O2
- SMILES
- COCC(C)O
- Molecular Weight1
- 90.12
- CAS
- 107-98-2
- Other Names
-
- 1-Methoxy-2-hydroxypropane
- 1-Methoxypropan-2-ol
- 1-methoxy-2-propanol
- 2-Methoxy-1-methylethanol
- Closol
- Dowanol-33B
- Dowtherm 209
- Glycol ether pm
- Icinol PM
- Methoxyisopropanol
- Methoxypropanol, «alpha» isomer
- NSC 2409
- PGME
- Poly-solv MPM
- Poly-solve MPM
- Propan-1-methoxy-2-ol
- Propan-2-ol, 1-methoxy-
- Propasol solvent M
- Propylene glycol 1-methyl ether
- Solvent PM
- Ucar solvent lm
- propylene glycol monomethyl ether
- «alpha»-Propylene glycol monomethyl ether
- 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).
- n0 : Refractive Index.
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- 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.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -261.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -415.62 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 3.61 | kJ/mol | Solid-L... |
| ΔvapH° | [46.20; 46.40] | kJ/mol |
|
| ΔvapH° | 46.20 | kJ/mol | NIST |
| ΔvapH° | 46.40 | kJ/mol | NIST |
| log10WS | 0.04 | Crippen Calculated Property | |
| logPoct/wat | 0.014 | Crippen Calculated Property | |
| McVol | 78.960 | ml/mol | McGowan Calculated Property |
| Pc | 4113.00 ± 10.00 | kPa | NIST |
| Inp | [634.00; 673.40] |
|
|
| Inp | 636.00 | NIST | |
| Inp | 634.00 | NIST | |
| Inp | 673.20 | NIST | |
| Inp | 673.40 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 673.00 | NIST | |
| I | [1108.00; 1160.00] |
|
|
| I | 1160.00 | NIST | |
| I | 1146.90 | NIST | |
| I | 1131.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1135.00 | NIST | |
| Tboil | [391.70; 394.15] | K |
|
| Tboil | 393.30 | K | Isobari... |
| Tboil | 393.15 | K | Isobari... |
| Tboil | 391.70 | K | NIST |
| Tboil | 394.15 | K | NIST |
| Tc | 579.80 ± 0.30 | K | NIST |
| Tfus | 202.89 | K | Joback Calculated Property |
| Vc | 0.290 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [154.70; 194.63] | J/mol×K | [405.08; 571.21] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 450 500 550 | ||||
| Cp,gas | 154.70 | J/mol×K | 405.08 | Joback Calculated Property |
| Cp,gas | 161.85 | J/mol×K | 432.77 | Joback Calculated Property |
| Cp,gas | 168.81 | J/mol×K | 460.46 | Joback Calculated Property |
| Cp,gas | 175.56 | J/mol×K | 488.15 | Joback Calculated Property |
| Cp,gas | 182.12 | J/mol×K | 515.84 | Joback Calculated Property |
| Cp,gas | 188.48 | J/mol×K | 543.52 | Joback Calculated Property |
| Cp,gas | 194.63 | J/mol×K | 571.21 | Joback Calculated Property |
| η | [0.0010690; 0.0017070] | Pa×s | [298.15; 318.15] |
|
| η | 0.0017070 | Pa×s | 298.15 | Excess ... |
| η | 0.0013060 | Pa×s | 308.15 | Excess ... |
| η | 0.0010690 | Pa×s | 318.15 | Excess ... |
| Pvap | [3.61; 739.81] | kPa | [313.15; 473.15] |
|
|
T(K) Vapor pressure (kPa) 0 100 200 300 400 500 600 700 800 350 400 450 | ||||
| Pvap | 3.61 | kPa | 313.15 | Vapor-L... |
| Pvap | 9.25 | kPa | 331.47 | Vapor-L... |
| Pvap | 10.01 | kPa | 333.15 | Vapor-L... |
| Pvap | 13.11 | kPa | 339.12 | Vapor-L... |
| Pvap | 15.00 | kPa | 342.30 | Supplem... |
| Pvap | 15.79 | kPa | 343.15 | Vapor-L... |
| Pvap | 19.25 | kPa | 347.62 | Vapor-L... |
| Pvap | 19.25 | kPa | 347.71 | Vapor-L... |
| Pvap | 22.64 | kPa | 351.56 | Vapor-L... |
| Pvap | 23.50 | kPa | 352.50 | Supplem... |
| Pvap | 23.74 | kPa | 352.64 | Vapor-L... |
| Pvap | 24.18 | kPa | 353.15 | Vapor-L... |
| Pvap | 24.17 | kPa | 353.15 | Vapor-L... |
| Pvap | 24.25 | kPa | 353.15 | Vapor-L... |
| Pvap | 26.69 | kPa | 355.59 | Vapor-L... |
| Pvap | 26.70 | kPa | 355.83 | Isobari... |
| Pvap | 29.35 | kPa | 357.89 | Vapor-L... |
| Pvap | 29.57 | kPa | 358.15 | Vapor-L... |
| Pvap | 32.00 | kPa | 360.10 | Supplem... |
| Pvap | 32.79 | kPa | 360.78 | Vapor-L... |
| Pvap | 35.72 | kPa | 362.93 | Vapor-L... |
| Pvap | 35.74 | kPa | 363.01 | Vapor-L... |
| Pvap | 36.03 | kPa | 363.15 | Vapor-L... |
| Pvap | 40.00 | kPa | 365.99 | Isobari... |
| Pvap | 42.10 | kPa | 367.40 | Supplem... |
| Pvap | 43.29 | kPa | 368.03 | Vapor-L... |
| Pvap | 43.48 | kPa | 368.23 | Vapor-L... |
| Pvap | 49.10 | kPa | 371.60 | Supplem... |
| Pvap | 50.45 | kPa | 373.15 | Vapor L... |
| Pvap | 48.55 | kPa | 373.15 | Vapor L... |
| Pvap | 48.26 | kPa | 373.15 | Vapor L... |
| Pvap | 52.16 | kPa | 373.15 | Vapor-L... |
| Pvap | 52.30 | kPa | 373.22 | Vapor-L... |
| Pvap | 52.31 | kPa | 373.31 | Vapor-L... |
| Pvap | 53.30 | kPa | 373.87 | Isobari... |
| Pvap | 57.60 | kPa | 376.00 | Supplem... |
| Pvap | 61.89 | kPa | 378.01 | Vapor-L... |
| Pvap | 66.10 | kPa | 380.00 | Supplem... |
| Pvap | 66.70 | kPa | 380.27 | Isobari... |
| Pvap | 74.60 | kPa | 383.50 | Supplem... |
| Pvap | 80.00 | kPa | 385.71 | Isobari... |
| Pvap | 83.30 | kPa | 386.90 | Supplem... |
| Pvap | 92.60 | kPa | 390.10 | Supplem... |
| Pvap | 93.30 | kPa | 390.45 | Isobari... |
| Pvap | 98.70 | kPa | 392.20 | Isobari... |
| Pvap | 99.90 | kPa | 392.80 | Supplem... |
| Pvap | 101.30 | kPa | 393.15 | Isobari... |
| Pvap | 116.90 | kPa | 397.90 | Supplem... |
| Pvap | 125.50 | kPa | 400.00 | Supplem... |
| Pvap | 134.00 | kPa | 402.20 | Supplem... |
| Pvap | 142.50 | kPa | 404.30 | Supplem... |
| Pvap | 151.00 | kPa | 406.30 | Supplem... |
| Pvap | 159.50 | kPa | 408.20 | Supplem... |
| Pvap | 168.00 | kPa | 410.00 | Supplem... |
| Pvap | 176.50 | kPa | 411.80 | Supplem... |
| Pvap | 230.60 | kPa | 423.15 | Vapor L... |
| Pvap | 232.93 | kPa | 423.15 | Vapor L... |
| Pvap | 232.13 | kPa | 423.15 | Vapor L... |
| Pvap | 231.95 | kPa | 423.15 | Vapor L... |
| Pvap | 739.81 | kPa | 473.15 | Vapor L... |
| n0 | 1.40100 | 298.15 | Density... | |
| csound,fluid | [104.80; 1298.14] | m/s | [288.15; 577.92] |
|
|
T(K) Speed of sound in fluid (m/s) 0 200 400 600 800 1000 1200 1400 300 400 500 | ||||
| csound,fluid | 1298.14 | m/s | 288.15 | Densiti... |
| csound,fluid | 1280.08 | m/s | 293.15 | Densiti... |
| csound,fluid | 1261.54 | m/s | 298.15 | Densiti... |
| csound,fluid | 1243.03 | m/s | 303.15 | Densiti... |
| csound,fluid | 1224.50 | m/s | 308.15 | Densiti... |
| csound,fluid | 828.20 | m/s | 412.24 | Speed o... |
| csound,fluid | 744.50 | m/s | 434.19 | Speed o... |
| csound,fluid | 670.70 | m/s | 453.43 | Speed o... |
| csound,fluid | 572.30 | m/s | 479.45 | Speed o... |
| csound,fluid | 486.90 | m/s | 500.92 | Speed o... |
| csound,fluid | 384.10 | m/s | 524.99 | Speed o... |
| csound,fluid | 304.10 | m/s | 542.86 | Speed o... |
| csound,fluid | 260.70 | m/s | 553.70 | Speed o... |
| csound,fluid | 231.80 | m/s | 558.23 | Speed o... |
| csound,fluid | 204.20 | m/s | 563.74 | Speed o... |
| csound,fluid | 158.10 | m/s | 570.21 | Speed o... |
| csound,fluid | 138.70 | m/s | 573.29 | Speed o... |
| csound,fluid | 104.80 | m/s | 577.92 | Speed o... |
Similar Compounds
![2-Propanol, 1-[2-(2-methoxy-1-methylethoxy)-1-methylethoxy]-.](data:image/png;base64,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)
![2-Propanol, 1,1'-[(1-methyl-1,2-ethanediyl)bis(oxy)]bis-.](data:image/png;base64,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)
Find more compounds similar to 2-Propanol, 1-methoxy-.
Mixtures
- 2-Propanol, 1-methoxy- + Water
- 1-Methoxy-2-propyl acetate + 2-Propanol, 1-methoxy-
- Acetic acid, methyl ester + 2-Propanol, 1-methoxy-
- 1-Propanol, 2-methoxy- + 2-Propanol, 1-methoxy-
- Benzenamine, 4-chloro-2,5-dimethoxy- + 2-Propanol, 1-methoxy-
- 1-Pentanamine + 2-Propanol, 1-methoxy-
- 2-Pyrrolidinone, 1-methyl- + 2-Propanol, 1-methoxy-
- Ethane, nitro- + 2-Propanol, 1-methoxy-
- Benzene + 2-Propanol, 1-methoxy-
- 2-Propanol, 1-methoxy- + Cyclohexane
- 2-Propenoic acid, 2-methyl- + 2-Propanol, 1-methoxy-
- Benzyl methacrylate + 2-Propanol, 1-methoxy-
- Ethyl Acetate + 2-Propanol, 1-methoxy-
- Acetic acid, butyl ester + 2-Propanol, 1-methoxy-
- Monoethanolamine + 2-Propanol, 1-methoxy-
- Furfural + 2-Propanol, 1-methoxy-
- Ethanol, 2-methoxy- + 2-Propanol, 1-methoxy-
- Dimethyl Sulfoxide + Sulfur dioxide + 2-Propanol, 1-methoxy-
- Sulfur dioxide + 2-Propanol, 1-methoxy-
- Toluene + 2-Propanol, 1-methoxy-
Find more mixtures with 2-Propanol, 1-methoxy-.
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
- Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
- Isobaric (vapor + liquid) equilibria for the binary systems (1-methoxy-2- propanol + 2-methoxyethanol), (2-butanone + 2-methoxyethanol) and (water + 2-methoxyethanol) at pressures of (74.5, 101.3, and 134.0) kPa
- Solubility Properties and Absorption Mechanism Investigation of Dilute SO2 in Propylene Glycol Monomethyl Ether + Dimethyl Sulfoxide System
- Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
- Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
- Solubility of 4-Chloro-2,5-dimethoxynitrobenzene, 4-Chloro-2,5-dimethoxyaniline, and 2,5-Dimethoxyaniline in Binary and Pure Solvents: Determination and Modeling
- Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
- Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
- Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
- Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
- Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
- Excess Molar Volumes and Viscosities for Binary Mixtures of Propylene Glycol Monomethyl Ether with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
- Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
- Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
- Solubilities of Three Phosphorus Flame Retardants in Selected Organic Solvents
- Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
- Joback Method
- McGowan Method
- NIST Webbook
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