- InChI
- InChI=1S/C6H14O2/c1-3-4-8-5-6(2)7/h6-7H,3-5H2,1-2H3
- InChI Key
- FENFUOGYJVOCRY-UHFFFAOYSA-N
- Formula
- C6H14O2
- SMILES
- CCCOCC(C)O
- Molecular Weight1
- 118.17
- CAS
- 1569-01-3
- Other Names
-
- 1-Propoxy-2-propanol
- 1-propoxypropan-2-ol
- Propasol solvent P
- Propylene glycol n-propyl ether
- Propylene glycol-n-monopropyl ether
- propane, 2-hydroxy-1-propoxy-
- propylene glycol, 1-propyl 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° | -244.62 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -456.90 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 13.05 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 47.65 | kJ/mol | Joback Calculated Property |
| log10WS | -0.80 | Crippen Calculated Property | |
| logPoct/wat | 0.794 | Crippen Calculated Property | |
| McVol | 107.140 | ml/mol | McGowan Calculated Property |
| Pc | 3415.86 | kPa | Joback Calculated Property |
| Inp | [797.00; 840.10] |
|
|
| Inp | 797.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 839.70 | NIST | |
| Inp | 840.10 | NIST | |
| I | 1263.80 | NIST | |
| Tboil | 422.95 | K | NIST |
| Tc | 615.45 | K | Joback Calculated Property |
| Tfus | 225.43 | K | Joback Calculated Property |
| Vc | 0.403 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [230.32; 283.50] | J/mol×K | [450.84; 615.45] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 230 240 250 260 270 280 450 500 550 600 | ||||
| Cp,gas | 230.32 | J/mol×K | 450.84 | Joback Calculated Property |
| Cp,gas | 239.95 | J/mol×K | 478.28 | Joback Calculated Property |
| Cp,gas | 249.26 | J/mol×K | 505.71 | Joback Calculated Property |
| Cp,gas | 258.28 | J/mol×K | 533.15 | Joback Calculated Property |
| Cp,gas | 266.99 | J/mol×K | 560.58 | Joback Calculated Property |
| Cp,gas | 275.39 | J/mol×K | 588.02 | Joback Calculated Property |
| Cp,gas | 283.50 | J/mol×K | 615.45 | Joback Calculated Property |
| Cp,liquid | [271.60; 302.40] | J/mol×K | [275.15; 339.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 270 275 280 285 290 295 300 305 280 300 320 340 | ||||
| Cp,liquid | 271.60 | J/mol×K | 275.15 | Heat ca... |
| Cp,liquid | 272.40 | J/mol×K | 276.65 | Heat ca... |
| Cp,liquid | 273.20 | J/mol×K | 278.15 | Heat ca... |
| Cp,liquid | 274.00 | J/mol×K | 279.65 | Heat ca... |
| Cp,liquid | 274.80 | J/mol×K | 281.15 | Heat ca... |
| Cp,liquid | 275.60 | J/mol×K | 282.65 | Heat ca... |
| Cp,liquid | 276.40 | J/mol×K | 284.15 | Heat ca... |
| Cp,liquid | 277.20 | J/mol×K | 285.65 | Heat ca... |
| Cp,liquid | 278.00 | J/mol×K | 287.15 | Heat ca... |
| Cp,liquid | 278.80 | J/mol×K | 288.65 | Heat ca... |
| Cp,liquid | 279.60 | J/mol×K | 290.15 | Heat ca... |
| Cp,liquid | 280.30 | J/mol×K | 291.65 | Heat ca... |
| Cp,liquid | 281.10 | J/mol×K | 293.15 | Heat ca... |
| Cp,liquid | 281.90 | J/mol×K | 294.65 | Heat ca... |
| Cp,liquid | 282.60 | J/mol×K | 296.15 | Heat ca... |
| Cp,liquid | 283.40 | J/mol×K | 297.65 | Heat ca... |
| Cp,liquid | 283.60 | J/mol×K | 298.15 | Heat ca... |
| Cp,liquid | 284.10 | J/mol×K | 299.15 | Heat ca... |
| Cp,liquid | 284.90 | J/mol×K | 300.65 | Heat ca... |
| Cp,liquid | 285.60 | J/mol×K | 302.15 | Heat ca... |
| Cp,liquid | 286.40 | J/mol×K | 303.65 | Heat ca... |
| Cp,liquid | 287.10 | J/mol×K | 305.15 | Heat ca... |
| Cp,liquid | 287.80 | J/mol×K | 306.65 | Heat ca... |
| Cp,liquid | 288.50 | J/mol×K | 308.15 | Heat ca... |
| Cp,liquid | 289.20 | J/mol×K | 309.65 | Heat ca... |
| Cp,liquid | 290.00 | J/mol×K | 311.15 | Heat ca... |
| Cp,liquid | 290.70 | J/mol×K | 312.65 | Heat ca... |
| Cp,liquid | 291.40 | J/mol×K | 314.15 | Heat ca... |
| Cp,liquid | 292.10 | J/mol×K | 315.65 | Heat ca... |
| Cp,liquid | 292.80 | J/mol×K | 317.15 | Heat ca... |
| Cp,liquid | 293.40 | J/mol×K | 318.65 | Heat ca... |
| Cp,liquid | 294.10 | J/mol×K | 320.15 | Heat ca... |
| Cp,liquid | 294.80 | J/mol×K | 321.65 | Heat ca... |
| Cp,liquid | 295.50 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 296.10 | J/mol×K | 324.65 | Heat ca... |
| Cp,liquid | 296.80 | J/mol×K | 326.15 | Heat ca... |
| Cp,liquid | 297.50 | J/mol×K | 327.65 | Heat ca... |
| Cp,liquid | 298.10 | J/mol×K | 329.15 | Heat ca... |
| Cp,liquid | 298.80 | J/mol×K | 330.65 | Heat ca... |
| Cp,liquid | 299.40 | J/mol×K | 332.15 | Heat ca... |
| Cp,liquid | 300.00 | J/mol×K | 333.65 | Heat ca... |
| Cp,liquid | 300.70 | J/mol×K | 335.15 | Heat ca... |
| Cp,liquid | 301.30 | J/mol×K | 336.65 | Heat ca... |
| Cp,liquid | 301.90 | J/mol×K | 338.15 | Heat ca... |
| Cp,liquid | 302.40 | J/mol×K | 339.15 | Heat ca... |
| η | [0.0001822; 0.0820702] | Pa×s | [225.43; 450.84] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 300 400 | ||||
| η | 0.0820702 | Pa×s | 225.43 | Joback Calculated Property |
| η | 0.0143235 | Pa×s | 263.00 | Joback Calculated Property |
| η | 0.0038675 | Pa×s | 300.57 | Joback Calculated Property |
| η | 0.0013969 | Pa×s | 338.13 | Joback Calculated Property |
| η | 0.0006185 | Pa×s | 375.70 | Joback Calculated Property |
| η | 0.0003176 | Pa×s | 413.27 | Joback Calculated Property |
| η | 0.0001822 | Pa×s | 450.84 | Joback Calculated Property |
| Pvap | [0.34; 74.98] | kPa | [298.15; 413.15] |
|
|
T(K) Vapor pressure (kPa) 0 10 20 30 40 50 60 70 80 300 350 400 | ||||
| Pvap | 0.34 | kPa | 298.15 | Isobari... |
| Pvap | 0.48 | kPa | 303.15 | Isobari... |
| Pvap | 0.67 | kPa | 308.15 | Isobari... |
| Pvap | 0.94 | kPa | 313.15 | Isobari... |
| Pvap | 1.27 | kPa | 318.15 | Isobari... |
| Pvap | 1.71 | kPa | 323.15 | Isobari... |
| Pvap | 2.26 | kPa | 328.15 | Isobari... |
| Pvap | 2.97 | kPa | 333.15 | Isobari... |
| Pvap | 3.84 | kPa | 338.15 | Isobari... |
| Pvap | 4.95 | kPa | 343.15 | Isobari... |
| Pvap | 6.29 | kPa | 348.15 | Isobari... |
| Pvap | 7.96 | kPa | 353.15 | Isobari... |
| Pvap | 9.95 | kPa | 358.15 | Isobari... |
| Pvap | 12.38 | kPa | 363.15 | Isobari... |
| Pvap | 15.27 | kPa | 368.15 | Isobari... |
| Pvap | 18.70 | kPa | 373.15 | Isobari... |
| Pvap | 22.65 | kPa | 378.15 | Isobari... |
| Pvap | 27.42 | kPa | 383.15 | Isobari... |
| Pvap | 32.80 | kPa | 388.15 | Isobari... |
| Pvap | 39.18 | kPa | 393.15 | Isobari... |
| Pvap | 46.38 | kPa | 398.15 | Isobari... |
| Pvap | 54.75 | kPa | 403.15 | Isobari... |
| Pvap | 64.10 | kPa | 408.15 | Isobari... |
| Pvap | 74.98 | kPa | 413.15 | Isobari... |
| ρl | [876.28; 894.46] | kg/m3 | [283.15; 303.15] |
|
|
T(K) Liquid Density (kg/m3) 875 880 885 890 895 285 290 295 300 | ||||
| ρl | 894.46 | kg/m3 | 283.15 | Volumet... |
| ρl | 889.96 | kg/m3 | 288.15 | Volumet... |
| ρl | 885.46 | kg/m3 | 293.15 | Volumet... |
| ρl | 880.84 | kg/m3 | 298.15 | Volumet... |
| ρl | 876.28 | kg/m3 | 303.15 | Volumet... |
| csound,fluid | [1211.05; 1301.94] | m/s | [283.15; 308.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1220 1240 1260 1280 1300 290 300 | ||||
| csound,fluid | 1301.94 | m/s | 283.15 | Ultraso... |
| csound,fluid | 1283.21 | m/s | 288.15 | Ultraso... |
| csound,fluid | 1282.87 | m/s | 288.15 | Densiti... |
| csound,fluid | 1264.52 | m/s | 293.15 | Ultraso... |
| csound,fluid | 1266.18 | m/s | 293.15 | Densiti... |
| csound,fluid | 1245.79 | m/s | 298.15 | Ultraso... |
| csound,fluid | 1247.82 | m/s | 298.15 | Densiti... |
| csound,fluid | 1227.33 | m/s | 303.15 | Ultraso... |
| csound,fluid | 1229.44 | m/s | 303.15 | Densiti... |
| csound,fluid | 1211.05 | m/s | 308.15 | Densiti... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 895.1 |
| 283.15 | 1000.00 | 895.7 |
| 283.15 | 2500.00 | 896.7 |
| 283.15 | 5000.00 | 898.5 |
| 283.15 | 7500.00 | 900.1 |
| 283.15 | 10000.00 | 901.8 |
| 283.15 | 15000.00 | 905.0 |
| 283.15 | 20000.00 | 908.1 |
| 283.15 | 25000.00 | 911.1 |
| 293.15 | 100.00 | 886.0 |
| 293.15 | 1000.00 | 886.6 |
| 293.15 | 2500.00 | 887.7 |
| 293.15 | 5000.00 | 889.6 |
| 293.15 | 7500.00 | 891.3 |
| 293.15 | 10000.00 | 893.1 |
| 293.15 | 15000.00 | 896.5 |
| 293.15 | 20000.00 | 899.8 |
| 293.15 | 25000.00 | 902.9 |
| 303.15 | 100.00 | 876.4 |
| 303.15 | 1000.00 | 877.2 |
| 303.15 | 2500.00 | 878.4 |
| 303.15 | 5000.00 | 880.3 |
| 303.15 | 7500.00 | 882.2 |
| 303.15 | 10000.00 | 884.0 |
| 303.15 | 15000.00 | 887.6 |
| 303.15 | 20000.00 | 891.1 |
| 303.15 | 25000.00 | 894.4 |
| 313.15 | 100.00 | 866.9 |
| 313.15 | 1000.00 | 867.6 |
| 313.15 | 2500.00 | 868.9 |
| 313.15 | 5000.00 | 871.0 |
| 313.15 | 7500.00 | 873.0 |
| 313.15 | 10000.00 | 875.0 |
| 313.15 | 15000.00 | 878.8 |
| 313.15 | 20000.00 | 882.4 |
| 313.15 | 25000.00 | 885.9 |
| 323.15 | 100.00 | 857.2 |
| 323.15 | 1000.00 | 858.0 |
| 323.15 | 2500.00 | 859.3 |
| 323.15 | 5000.00 | 861.4 |
| 323.15 | 7500.00 | 863.5 |
| 323.15 | 10000.00 | 865.6 |
| 323.15 | 15000.00 | 869.6 |
| 323.15 | 20000.00 | 873.5 |
| 323.15 | 25000.00 | 877.2 |
| 333.15 | 100.00 | 847.1 |
| 333.15 | 1000.00 | 847.9 |
| 333.15 | 2500.00 | 849.3 |
| 333.15 | 5000.00 | 851.7 |
| 333.15 | 7500.00 | 853.9 |
| 333.15 | 10000.00 | 856.1 |
| 333.15 | 15000.00 | 860.3 |
| 333.15 | 20000.00 | 864.3 |
| 333.15 | 25000.00 | 868.1 |
| 343.15 | 100.00 | 837.5 |
| 343.15 | 1000.00 | 838.4 |
| 343.15 | 2500.00 | 840.0 |
| 343.15 | 5000.00 | 842.4 |
| 343.15 | 7500.00 | 844.9 |
| 343.15 | 10000.00 | 847.2 |
| 343.15 | 15000.00 | 851.8 |
| 343.15 | 20000.00 | 856.0 |
| 343.15 | 25000.00 | 860.1 |
| 353.15 | 100.00 | 827.3 |
| 353.15 | 1000.00 | 828.3 |
| 353.15 | 2500.00 | 829.9 |
| 353.15 | 5000.00 | 832.6 |
| 353.15 | 7500.00 | 835.2 |
| 353.15 | 10000.00 | 837.7 |
| 353.15 | 15000.00 | 842.5 |
| 353.15 | 20000.00 | 847.0 |
| 353.15 | 25000.00 | 851.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [323.58; 446.21] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.61743e+01 | |||
| Coefficient B | -4.21246e+03 | |||
| Coefficient C | -5.84240e+01 | |||
| Temperature range, min. | 323.58 | |||
| Temperature range, max. | 446.21 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
| Pvap | 1.33 | kPa | 323.58 | Calculated Property |
| Pvap | 2.90 | kPa | 337.21 | Calculated Property |
| Pvap | 5.86 | kPa | 350.83 | Calculated Property |
| Pvap | 11.13 | kPa | 364.46 | Calculated Property |
| Pvap | 20.01 | kPa | 378.08 | Calculated Property |
| Pvap | 34.30 | kPa | 391.71 | Calculated Property |
| Pvap | 56.35 | kPa | 405.33 | Calculated Property |
| Pvap | 89.16 | kPa | 418.96 | Calculated Property |
| Pvap | 136.44 | kPa | 432.58 | Calculated Property |
| Pvap | 202.65 | kPa | 446.21 | Calculated Property |
Similar Compounds
![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-propoxy-.
Mixtures
- 2-Propanol, 1-propoxy- + Methyl Alcohol
- 2-Propanol, 1-propoxy- + Ethanol
- 2-Propanol, 1-propoxy- + 1-Hexanol
- 2-Propanol, 1-propoxy- + Water
- 2-Propanol, 1-propoxy- + Acetic acid, methyl ester
- 2-Propanol, 1-propoxy- + Ethyl Acetate
- 2-Propanol, 1-propoxy- + Acetic acid, butyl ester
- 2-Propanol, 1-propoxy- + Decane + Water
- 2-Propanol, 1-propoxy- + Dodecane + Water
- 2-Propanol, 1-propoxy- + Hexadecane + Water
- 2-Propanol, 1-propoxy- + Tetradecane + Water
Sources
- Crippen Method
- Crippen Method
- Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
- Phase behavior of glycol ether surfactant systems in the presence of brine and hydrocarbon: Experiment and modeling
- Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
- Volumetric properties of (1-propoxypropan-2-ol + water) mixtures between (283 and 303) K: The effect of branching on alkoxyalcohols
- Ultrasound speeds and molar isentropic compressions of aqueous 1-propoxypropan-2-ol mixtures from T = (283.15 to 303.15) K. Influence of solute structure
- (Liquid + liquid) equilibria for the ternary system (water + dodecane + propylene glycol n-propyl ether)
- Water activity in 1-propoxypropan-2-ol aqueous mixtures at T = 298 K
- Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
- PpT Measurements and EoS Predictions of Glycol Ethers from (283.15 to 353.15) K at Pressures up to 25 MPa
- Liquid-Liquid Equilibria for the Ternary System Water + Hexadecane + Propylene Glycol n-Propyl Ether
- Liquid Liquid Equilibria for the Ternary System Water + Tetradecane + Propylene Glycol n-Propyl Ether
- 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
- Solubilities of Three Phosphorus Flame Retardants in Selected Organic Solvents
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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