- InChI
- InChI=1S/C5H12O2/c1-2-4-7-5-3-6/h6H,2-5H2,1H3
- InChI Key
- YEYKMVJDLWJFOA-UHFFFAOYSA-N
- Formula
- C5H12O2
- SMILES
- CCCOCCO
- Molecular Weight1
- 104.15
- CAS
- 2807-30-9
- Other Names
-
- 2-Propoxyethanol
- 2-Propyloxyethanol
- 3-Oxa-1-hexanol
- Eastman EP
- Ektasolve EP
- Ethylene glycol monopropyl ether
- Ethylene glycol propyl ether
- Ethyleneglycol mono-n-propyl ether
- Monopropyl ether of ethylene glycol
- Propoxyethanol
- Propyl cellosolve
- Propyl glycol
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (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).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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° | -250.60 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -430.98 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 13.98 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [52.10; 52.13] | kJ/mol |
|
| ΔvapH° | 52.13 | kJ/mol | NIST |
| ΔvapH° | 52.10 ± 0.10 | kJ/mol | NIST |
| log10WS | -0.27 | Crippen Calculated Property | |
| logPoct/wat | 0.405 | Crippen Calculated Property | |
| McVol | 93.050 | ml/mol | McGowan Calculated Property |
| Pc | 3650.00 ± 20.00 | kPa | NIST |
| ρc | 286.41 ± 6.25 | kg/m3 | NIST |
| Inp | [790.00; 819.00] |
|
|
| Inp | 819.00 | NIST | |
| Inp | 800.70 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 800.70 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 809.00 | NIST | |
| I | [1325.90; 1325.90] |
|
|
| I | 1325.90 | NIST | |
| I | 1325.90 | NIST | |
| Tboil | [422.90; 424.50] | K |
|
| Tboil | 422.90 | K | NIST |
| Tboil | 424.50 ± 0.60 | K | NIST |
| Tc | [614.60; 615.20] | K |
|
| Tc | 615.20 ± 1.00 | K | NIST |
| Tc | 614.60 ± 0.50 | K | NIST |
| Tfus | 229.16 | K | Joback Calculated Property |
| Vc | 0.352 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [191.25; 236.84] | J/mol×K | [428.40; 590.36] |
|
| Cp,gas | 191.25 | J/mol×K | 428.40 | Joback Calculated Property |
| Cp,gas | 199.44 | J/mol×K | 455.39 | Joback Calculated Property |
| Cp,gas | 207.39 | J/mol×K | 482.39 | Joback Calculated Property |
| Cp,gas | 215.11 | J/mol×K | 509.38 | Joback Calculated Property |
| Cp,gas | 222.59 | J/mol×K | 536.37 | Joback Calculated Property |
| Cp,gas | 229.83 | J/mol×K | 563.36 | Joback Calculated Property |
| Cp,gas | 236.84 | J/mol×K | 590.36 | Joback Calculated Property |
| Cp,liquid | [231.60; 259.90] | J/mol×K | [275.15; 339.15] |
|
| Cp,liquid | 231.60 | J/mol×K | 275.15 | Measure... |
| Cp,liquid | 232.40 | J/mol×K | 277.15 | Measure... |
| Cp,liquid | 233.30 | J/mol×K | 279.15 | Measure... |
| Cp,liquid | 234.10 | J/mol×K | 281.15 | Measure... |
| Cp,liquid | 235.00 | J/mol×K | 283.15 | Measure... |
| Cp,liquid | 235.80 | J/mol×K | 285.15 | Measure... |
| Cp,liquid | 236.60 | J/mol×K | 287.15 | Measure... |
| Cp,liquid | 237.50 | J/mol×K | 289.15 | Measure... |
| Cp,liquid | 238.30 | J/mol×K | 291.15 | Measure... |
| Cp,liquid | 239.20 | J/mol×K | 293.15 | Measure... |
| Cp,liquid | 240.10 | J/mol×K | 295.15 | Measure... |
| Cp,liquid | 240.90 | J/mol×K | 297.15 | Measure... |
| Cp,liquid | 241.40 | J/mol×K | 298.15 | Measure... |
| Cp,liquid | 244.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 241.78 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 241.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 241.80 | J/mol×K | 299.15 | Measure... |
| Cp,liquid | 242.70 | J/mol×K | 301.15 | Measure... |
| Cp,liquid | 243.50 | J/mol×K | 303.15 | Measure... |
| Cp,liquid | 244.40 | J/mol×K | 305.15 | Measure... |
| Cp,liquid | 245.30 | J/mol×K | 307.15 | Measure... |
| Cp,liquid | 246.20 | J/mol×K | 309.15 | Measure... |
| Cp,liquid | 247.10 | J/mol×K | 311.15 | Measure... |
| Cp,liquid | 248.00 | J/mol×K | 313.15 | Measure... |
| Cp,liquid | 248.90 | J/mol×K | 315.15 | Measure... |
| Cp,liquid | 249.80 | J/mol×K | 317.15 | Measure... |
| Cp,liquid | 250.70 | J/mol×K | 319.15 | Measure... |
| Cp,liquid | 251.60 | J/mol×K | 321.15 | Measure... |
| Cp,liquid | 252.50 | J/mol×K | 323.15 | Measure... |
| Cp,liquid | 253.40 | J/mol×K | 325.15 | Measure... |
| Cp,liquid | 254.30 | J/mol×K | 327.15 | Measure... |
| Cp,liquid | 255.20 | J/mol×K | 329.15 | Measure... |
| Cp,liquid | 256.10 | J/mol×K | 331.15 | Measure... |
| Cp,liquid | 257.10 | J/mol×K | 333.15 | Measure... |
| Cp,liquid | 258.00 | J/mol×K | 335.15 | Measure... |
| Cp,liquid | 258.90 | J/mol×K | 337.15 | Measure... |
| Cp,liquid | 259.90 | J/mol×K | 339.15 | Measure... |
| η | [0.0002268; 0.0464966] | Pa×s | [229.16; 428.40] |
|
| η | 0.0464966 | Pa×s | 229.16 | Joback Calculated Property |
| η | 0.0109215 | Pa×s | 262.37 | Joback Calculated Property |
| η | 0.0035523 | Pa×s | 295.57 | Joback Calculated Property |
| η | 0.0014496 | Pa×s | 328.78 | Joback Calculated Property |
| η | 0.0006973 | Pa×s | 361.99 | Joback Calculated Property |
| η | 0.0003793 | Pa×s | 395.19 | Joback Calculated Property |
| η | 0.0002268 | Pa×s | 428.40 | Joback Calculated Property |
| ΔvapH | [41.40; 46.30] | kJ/mol | [386.00; 422.90] |
|
| ΔvapH | 46.30 | kJ/mol | 386.00 | NIST |
| ΔvapH | 41.40 | kJ/mol | 422.90 | NIST |
| Pvap | [0.45; 100.00] | kPa | [303.15; 422.75] |
|
| Pvap | 0.45 | kPa | 303.15 | Measure... |
| Pvap | 0.89 | kPa | 313.15 | Measure... |
| Pvap | 0.87 | kPa | 313.15 | Measure... |
| Pvap | 1.59 | kPa | 323.15 | Measure... |
| Pvap | 1.61 | kPa | 323.15 | Measure... |
| Pvap | 60.00 | kPa | 406.13 | Isobari... |
| Pvap | 60.00 | kPa | 406.15 | Isobari... |
| Pvap | 60.00 | kPa | 406.15 | Isobari... |
| Pvap | 80.00 | kPa | 415.28 | Isobari... |
| Pvap | 80.00 | kPa | 415.30 | Isobari... |
| Pvap | 80.00 | kPa | 415.30 | Isobari... |
| Pvap | 100.00 | kPa | 422.73 | Isobari... |
| Pvap | 100.00 | kPa | 422.75 | Isobari... |
| Pvap | 100.00 | kPa | 422.75 | Isobari... |
| ρl | [881.49; 908.31] | kg/m3 | [298.15; 328.15] |
|
| ρl | 907.23 | kg/m3 | 298.15 | Thermod... |
| ρl | 908.31 | kg/m3 | 298.15 | Study o... |
| ρl | 907.88 | kg/m3 | 298.15 | Modifie... |
| ρl | 908.00 | kg/m3 | 298.15 | An expe... |
| ρl | 903.00 | kg/m3 | 303.15 | An expe... |
| ρl | 899.50 | kg/m3 | 308.15 | Study o... |
| ρl | 899.00 | kg/m3 | 308.15 | An expe... |
| ρl | 895.00 | kg/m3 | 313.15 | An expe... |
| ρl | 890.56 | kg/m3 | 318.15 | Study o... |
| ρl | 890.00 | kg/m3 | 318.15 | An expe... |
| ρl | 881.49 | kg/m3 | 328.15 | Study o... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 423.20 | K | 99.10 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [325.70; 445.45] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.64940e+01 | |||
| Coefficient B | -4.31962e+03 | |||
| Coefficient C | -5.91610e+01 | |||
| Temperature range, min. | 325.70 | |||
| Temperature range, max. | 445.45 | |||
| Pvap | 1.33 | kPa | 325.70 | Calculated Property |
| Pvap | 2.88 | kPa | 339.01 | Calculated Property |
| Pvap | 5.81 | kPa | 352.31 | Calculated Property |
| Pvap | 11.01 | kPa | 365.62 | Calculated Property |
| Pvap | 19.79 | kPa | 378.92 | Calculated Property |
| Pvap | 33.94 | kPa | 392.23 | Calculated Property |
| Pvap | 55.86 | kPa | 405.53 | Calculated Property |
| Pvap | 88.61 | kPa | 418.84 | Calculated Property |
| Pvap | 136.00 | kPa | 432.14 | Calculated Property |
| Pvap | 202.67 | kPa | 445.45 | Calculated Property |
Similar Compounds
![2-[3-(2-Methoxyethoxy)propoxy]ethanol.](data:image/png;base64,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)
Find more compounds similar to Ethanol, 2-propoxy-.
Mixtures
- n-Hexane + Ethanol, 2-propoxy-
- Ethanol, 2-propoxy- + Heptane
- Diethyl carbonate + Ethanol, 2-propoxy-
- Ethanol, 2-propoxy- + Phosphonic acid, phenyl-
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- Ethanol, 2-propoxy- + 1-Butanol
- Ethanol, 2-propoxy- + Isopropyl Alcohol
- Ethanol, 2-propoxy- + Octane
- Ethanol, 2-propoxy- + sodium chloride + Water
Sources
- Crippen Method
- Crippen Method
- Isobaric vapor-liquid equilibria for the n-heptane + ethylene glycol monopropyl ether and n-octane + ethylene glycol monopropyl ether systems
- Temperature dependence of ternary phase diagrams for water + sodium chloride + ethylene glycol monopropyl ether at atmospheric pressure
- Thermodynamic properties and sPC-SAFT modeling of 2-ethoxyethanol, 2-propoxyethanol and 2-butoxyethanol from T = (293.15-413.15) K and pressure up to 30 MPa
- Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
- Study of thermophysical properties of the binary mixtures of ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate and 2-propoxyethanol from T = (298.15 to 328.15) K at atmospheric pressure
- Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
- An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
- Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
- Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
- Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
- Isobaric Vapor Liquid Equilibria for the 1-Propanol + Ethylene Glycol Monopropyl Ether and 1-Butanol + Ethylene Glycol Monopropyl Ether Systems
- Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
- 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.