- InChI
- InChI=1S/C7H16O2/c1-3-4-5-9-6-7(2)8/h7-8H,3-6H2,1-2H3
- InChI Key
- RWNUSVWFHDHRCJ-UHFFFAOYSA-N
- Formula
- C7H16O2
- SMILES
- CCCCOCC(C)O
- Molecular Weight1
- 132.20
- CAS
- 5131-66-8
- Other Names
-
- 1,2-Propylene glycol 1-monobutyl ether
- 1-Butoxy-2-propanol
- 1-butoxypropan-2-ol
- 2-Hydroxy-3-butoxypropane
- NSC 2211
- Propasol solvent B
- Propylene glycol monobutyl ether
- Propylene glycol n-butyl ether
- n-Butoxypropanol
- propane, 1-butoxy-2-hydroxy-
- propyleneglycol, 1-butyl ether
- 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).
- 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.
- 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° | -236.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -477.54 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.64 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 49.88 | kJ/mol | Joback Calculated Property |
| log10WS | -1.22 | Crippen Calculated Property | |
| logPoct/wat | 1.184 | Crippen Calculated Property | |
| McVol | 121.230 | ml/mol | McGowan Calculated Property |
| Pc | 3062.55 | kPa | Joback Calculated Property |
| Inp | [923.00; 948.00] |
|
|
| Inp | 936.20 | NIST | |
| Inp | 936.70 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | Outlier 923.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 936.20 | NIST | |
| I | 1363.50 | NIST | |
| Tboil | 443.35 | K | NIST |
| Tc | 637.45 | K | Joback Calculated Property |
| Tfus | 236.70 | K | Joback Calculated Property |
| Vc | 0.459 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [271.52; 330.41] | J/mol×K | [473.72; 637.45] |
|
| Cp,gas | 271.52 | J/mol×K | 473.72 | Joback Calculated Property |
| Cp,gas | 282.22 | J/mol×K | 501.01 | Joback Calculated Property |
| Cp,gas | 292.56 | J/mol×K | 528.30 | Joback Calculated Property |
| Cp,gas | 302.54 | J/mol×K | 555.59 | Joback Calculated Property |
| Cp,gas | 312.18 | J/mol×K | 582.87 | Joback Calculated Property |
| Cp,gas | 321.47 | J/mol×K | 610.16 | Joback Calculated Property |
| Cp,gas | 330.41 | J/mol×K | 637.45 | Joback Calculated Property |
| Cp,liquid | [302.30; 335.50] | J/mol×K | [275.15; 339.15] |
|
| Cp,liquid | 302.30 | J/mol×K | 275.15 | Heat ca... |
| Cp,liquid | 303.20 | J/mol×K | 276.65 | Heat ca... |
| Cp,liquid | 304.10 | J/mol×K | 278.15 | Heat ca... |
| Cp,liquid | 305.00 | J/mol×K | 279.65 | Heat ca... |
| Cp,liquid | 305.90 | J/mol×K | 281.15 | Heat ca... |
| Cp,liquid | 306.80 | J/mol×K | 282.65 | Heat ca... |
| Cp,liquid | 307.60 | J/mol×K | 284.15 | Heat ca... |
| Cp,liquid | 308.50 | J/mol×K | 285.65 | Heat ca... |
| Cp,liquid | 309.30 | J/mol×K | 287.15 | Heat ca... |
| Cp,liquid | 310.20 | J/mol×K | 288.65 | Heat ca... |
| Cp,liquid | 311.00 | J/mol×K | 290.15 | Heat ca... |
| Cp,liquid | 311.90 | J/mol×K | 291.65 | Heat ca... |
| Cp,liquid | 312.70 | J/mol×K | 293.15 | Heat ca... |
| Cp,liquid | 313.50 | J/mol×K | 294.65 | Heat ca... |
| Cp,liquid | 314.40 | J/mol×K | 296.15 | Heat ca... |
| Cp,liquid | 315.20 | J/mol×K | 297.65 | Heat ca... |
| Cp,liquid | 315.50 | J/mol×K | 298.15 | Heat ca... |
| Cp,liquid | 316.00 | J/mol×K | 299.15 | Heat ca... |
| Cp,liquid | 316.80 | J/mol×K | 300.65 | Heat ca... |
| Cp,liquid | 317.60 | J/mol×K | 302.15 | Heat ca... |
| Cp,liquid | 318.40 | J/mol×K | 303.65 | Heat ca... |
| Cp,liquid | 319.20 | J/mol×K | 305.15 | Heat ca... |
| Cp,liquid | 320.00 | J/mol×K | 306.65 | Heat ca... |
| Cp,liquid | 320.70 | J/mol×K | 308.15 | Heat ca... |
| Cp,liquid | 321.50 | J/mol×K | 309.65 | Heat ca... |
| Cp,liquid | 322.30 | J/mol×K | 311.15 | Heat ca... |
| Cp,liquid | 323.00 | J/mol×K | 312.65 | Heat ca... |
| Cp,liquid | 323.80 | J/mol×K | 314.15 | Heat ca... |
| Cp,liquid | 324.50 | J/mol×K | 315.65 | Heat ca... |
| Cp,liquid | 325.30 | J/mol×K | 317.15 | Heat ca... |
| Cp,liquid | 326.00 | J/mol×K | 318.65 | Heat ca... |
| Cp,liquid | 326.80 | J/mol×K | 320.15 | Heat ca... |
| Cp,liquid | 327.50 | J/mol×K | 321.65 | Heat ca... |
| Cp,liquid | 328.20 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 328.90 | J/mol×K | 324.65 | Heat ca... |
| Cp,liquid | 329.60 | J/mol×K | 326.15 | Heat ca... |
| Cp,liquid | 330.30 | J/mol×K | 327.65 | Heat ca... |
| Cp,liquid | 331.00 | J/mol×K | 329.15 | Heat ca... |
| Cp,liquid | 331.70 | J/mol×K | 330.65 | Heat ca... |
| Cp,liquid | 332.40 | J/mol×K | 332.15 | Heat ca... |
| Cp,liquid | 333.10 | J/mol×K | 333.65 | Heat ca... |
| Cp,liquid | 333.80 | J/mol×K | 335.15 | Heat ca... |
| Cp,liquid | 334.40 | J/mol×K | 336.65 | Heat ca... |
| Cp,liquid | 335.10 | J/mol×K | 338.15 | Heat ca... |
| Cp,liquid | 335.50 | J/mol×K | 339.15 | Heat ca... |
| η | [0.0001517; 0.0625947] | Pa×s | [236.70; 473.72] |
|
| η | 0.0625947 | Pa×s | 236.70 | Joback Calculated Property |
| η | 0.0111917 | Pa×s | 276.20 | Joback Calculated Property |
| η | 0.0030786 | Pa×s | 315.71 | Joback Calculated Property |
| η | 0.0011285 | Pa×s | 355.21 | Joback Calculated Property |
| η | 0.0005057 | Pa×s | 394.71 | Joback Calculated Property |
| η | 0.0002622 | Pa×s | 434.22 | Joback Calculated Property |
| η | 0.0001517 | Pa×s | 473.72 | Joback Calculated Property |
| ρl | [861.24; 879.03] | kg/m3 | [293.15; 313.15] |
|
| ρl | 879.03 | kg/m3 | 293.15 | Molecul... |
| ρl | 874.63 | kg/m3 | 298.15 | Molecul... |
| ρl | 870.20 | kg/m3 | 303.15 | Molecul... |
| ρl | 865.74 | kg/m3 | 308.15 | Molecul... |
| ρl | 861.24 | kg/m3 | 313.15 | Molecul... |
| csound,fluid | [1207.02; 1297.59] | m/s | [288.15; 313.15] |
|
| csound,fluid | 1297.59 | m/s | 288.15 | Densiti... |
| csound,fluid | 1278.98 | m/s | 293.15 | Thermod... |
| csound,fluid | 1279.95 | m/s | 293.15 | Densiti... |
| csound,fluid | 1260.90 | m/s | 298.15 | Thermod... |
| csound,fluid | 1261.87 | m/s | 298.15 | Densiti... |
| csound,fluid | 1242.94 | m/s | 303.15 | Thermod... |
| csound,fluid | 1243.85 | m/s | 303.15 | Densiti... |
| csound,fluid | 1224.91 | m/s | 308.15 | Thermod... |
| csound,fluid | 1225.83 | m/s | 308.15 | Densiti... |
| csound,fluid | 1207.02 | m/s | 313.15 | Thermod... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [341.82; 466.94] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.64361e+01 | |||
| Coefficient B | -4.47407e+03 | |||
| Coefficient C | -6.47630e+01 | |||
| Temperature range, min. | 341.82 | |||
| Temperature range, max. | 466.94 | |||
| Pvap | 1.33 | kPa | 341.82 | Calculated Property |
| Pvap | 2.88 | kPa | 355.72 | Calculated Property |
| Pvap | 5.81 | kPa | 369.62 | Calculated Property |
| Pvap | 11.03 | kPa | 383.53 | Calculated Property |
| Pvap | 19.83 | kPa | 397.43 | Calculated Property |
| Pvap | 34.00 | kPa | 411.33 | Calculated Property |
| Pvap | 55.95 | kPa | 425.23 | Calculated Property |
| Pvap | 88.70 | kPa | 439.14 | Calculated Property |
| Pvap | 136.07 | kPa | 453.04 | Calculated Property |
| Pvap | 202.66 | kPa | 466.94 | Calculated Property |
Similar Compounds
![Ethanol, 2-[2-(2-butoxyethoxy)ethoxy]-.](data:image/png;base64,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)
Find more compounds similar to 2-Propanol, 1-butoxy-.
Mixtures
- 1-Propanol + 2-Propanol, 1-butoxy-
- Isopropyl Alcohol + 2-Propanol, 1-butoxy-
- 1-Butanol + 2-Propanol, 1-butoxy-
- 2-Propanol, 1-butoxy- + 1-Hexanol
- 1-Octanol + 2-Propanol, 1-butoxy-
- 2-Propanol, 1-butoxy- + 1-Decanol
- 2-Propanol, 1-butoxy- + Acetic acid, methyl ester
- Ethyl Acetate + 2-Propanol, 1-butoxy-
- Acetic acid, butyl ester + 2-Propanol, 1-butoxy-
- 2-Propanol, 1-butoxy- + Water
Sources
- Crippen Method
- Crippen Method
- Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
- Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
- Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
- Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
- 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
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.