- InChI
- InChI=1S/C7H14O3/c1-3-9-6-5-7(8)10-4-2/h3-6H2,1-2H3
- InChI Key
- BHXIWUJLHYHGSJ-UHFFFAOYSA-N
- Formula
- C7H14O3
- SMILES
- CCOCCC(=O)OCC
- Molecular Weight1
- 146.19
- Other Names
-
- 3-Ethoxypropionic acid ethyl ester
- Ektapro EEP
- Ethoxypropionic acid, ethyl ester
- Ethyl 3-ethoxypropanoate
- Ethyl ester of 3-ethoxypropanoic acid
- Ethyl «beta»-ethoxypropionate
- Ethylester kyseliny 3-ethoxypropionove
- NSC 8870
- Propionic acid, 3-ethoxy-, ethyl ester
- Propionic acid,beta ethoxy,ethyl ester
- ethyl .beta.-ethoxypropionate
- ethyl 3-ethoxypropionate
- ethyl 4-oxahexanoate
- «beta»-Ethoxypropionic acid ethyl ester
- ω : Acentric Factor.
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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).
- ρc : Critical density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5149 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ΔfG° | -407.31 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -640.49 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 19.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 55.85 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.66 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.34 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.976 | Crippen Calculated Property | |
| McVol | 122.800 | ml/mol | McGowan Calculated Property |
| Pc | [2659.78; 2660.00] | kPa |
|
| Pc | 2660.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 2659.78 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 2660.00 ± 20.00 | kPa | NIST |
| ρc | 318.68 ± 5.85 | kg/m3 | NIST |
| Inp | [970.70; 970.70] |
|
|
| Inp | 970.70 | NIST | |
| Inp | 970.70 | NIST | |
| Ip | [1320.00; 1351.00] |
|
|
| Ip | 1332.00 | NIST | |
| Ip | 1351.00 | NIST | |
| Ip | 1320.00 | NIST | |
| Ip | 1332.00 | NIST | |
| Tboil | 436.58 | K | Relay (1.0) Calculated Property |
| Tc | [618.70; 621.00] | K |
|
| Tc | 621.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 618.70 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 621.00 ± 1.00 | K | NIST |
| Tc | 618.70 ± 2.00 | K | NIST |
| Tfus | 173.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | [0.458; 0.458] | m3/kmol |
|
| Vc | 0.458 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Vc | 0.458 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Zc | 0.2360000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0008590; 0.0011760] | Pa×s | [298.15; 318.15] |
|
| η | 0.0011760 | Pa×s | 298.15 | Density and Viscosity for Ethyl 3-Ethoxypropionate + Methacrylic Acid, + Benzyl Methacrylate, and + 2-Hydroxyethyl Methacrylate |
| η | 0.0009960 | Pa×s | 308.15 | Density and Viscosity for Ethyl 3-Ethoxypropionate + Methacrylic Acid, + Benzyl Methacrylate, and + 2-Hydroxyethyl Methacrylate |
| η | 0.0008590 | Pa×s | 318.15 | Density and Viscosity for Ethyl 3-Ethoxypropionate + Methacrylic Acid, + Benzyl Methacrylate, and + 2-Hydroxyethyl Methacrylate |
| ΔvapH | 45.50 | kJ/mol | 379.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [185.72; 407.07] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.74340e+01 | |||
| Coefficient B | 5.50840e-01 | |||
| Coefficient C | -1.51400e-04 | |||
| Coefficient D | -3.98000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 185.72 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 221.60 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 254.95 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 285.65 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 313.57 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 338.58 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 360.56 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 379.39 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 394.94 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 407.07 | J/mol×K | 1000.00 | Calculated Property |
Similar Compounds
![2-(2-[2-(Propionyloxy)ethoxy]ethoxy)ethyl propionate.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAO8klEQVR4nO3dfVBU1xnH8efC8qJiABMCBYJGk4CjIWYkqImKRNTY0HGmKXbMdDutrTvTmuBLMkM7zbjYpnGbjimxNiPDTCI6sRH/kpg0ERsJakwiRMAaMi0YFVINEllEdoFl9+kfZ10N6L5x7bJ5fp+/dsL17IH97rnnXl6iMTMByBAR6gkA/P8gdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB3C3oYNG5YsWdLW1ubzSMP/YTbe/POftGMH3XUX9fTQ9u00aVKI5wNh6MiRIw0NDVar1eeRoc79D3+gQ4fIYKDDh+mVV+jFF0M8HwhDBoOBiIaGhnweGdLNzJUrNGkSGQxERHPmUHNzKCcDYUvl7nA4fB4Z0tzj4shzAurooJSUUE4GwlZUVBT5t7qHdDMTEUGPP06bN1NuLlVUkNkcyslA2PJ/MxPqvfsLL9DJk/Tll7RlC6WmhngyEJ7U6j7mNzPMpGk0ezalplJWFi1dGsrJQNgKk0tVTaPISGKmiAgiIj/enQAjhcmlKpH7toymERH58e4EGMn/S9VQ5x4Vdf0xcoeghMlmhr69umMzA0EJk0tVwmYGdBA+q7vazDATIXcIUvit7hwf74qNDfFkIDyFzeo+1WDQiOqZI3p6Urq7QzsZCFNhcyMy6oY7M/5MF8LSxYtUX099fbdp+LC5Eanel8xM/k0Xws/rr9OmTdTYSKtW0enTt+95+vv7fR4T4p+ZUe/L8M69pYX27KGYGPr5zyktLdSzCQYzX7lyJT4+/raMvmsXHT5Mmkb5+fTHP9Lrr+s7fFtbW0VFBRF9/PHHPg8eQ6t7WG5mOjpo40b69a+pqIiMRrLbb8eTVFRUbN261el03o7BGxsbc3JykpOTTSaTXff5Dw7S+PHuG81TplBHh45j2+32TZs2zZw502q1GgyGZ555xve/4ZCaO3cuER0/flzTNCJyuVy6P4XT6dy5c+enn36q+8jMzDt28L597scvvsgffKDv8K2trcuWLdM0beLEidOnT6+qqtJx8O7u7meffTYyMtITQ0ZGxu7du51Opw6jOxy8Ywfb7bxoEQ8NMTM3NfHatXzwIP/lLzwwMMrhq6ur7733XiLSNM1oNJ49e9aff+VX7k6n0+FwjG56Nzd//nwiSk1NjYiIIKLBwUF9x29qapo/f35CQoKmaWvWrPn666/1HZ+3beP9+92P//xnfu891ulTsNlsmzZtio2NJaLY2NjExERV5NKlS5uamkY5uMvlqqysTE5OJiKDwVBcXLxr166HH35YPcXs2bM/GOX7tq6OH3yQibi0lN9+m596is1m/sEP+MwZnjGDifi++3jfPg5qdWttbX3yySfVVGfNmnX06FH//61fub/xxhuZmZn6Li3M3N7ennLDbzBFRERs3759SK0Eo2a1WtetW6c2S7GxsertlJCQ8PLLL9vt9tGO7nBwWRn/8pfc3Mw//Sm7XNzfz8uX81df8f33c3Exd3ePZvhhS9fFixcHBwfLy8uTkpLUF6qoqMjP9WykxsZGtcoQ0cKFC5ubm9V/d7lcVVVVU6ZMUR8qKCjwfCgAFy7wT37CmuZu+r33mJkHB/m//3UfUFPD2dlMxEScm8t1df6PbbPZzGazWgISEhLKysoCrcWv3PPz89WXID8/v6GhIaAnuCm73V5aWjpu3Dgiio+PX7FixezZs9VTPPTQQwcPHhzl+NXV1enp6Z6ly2q1fv7550VFReop7rnnnvLy8uBP2XV111+whgbeu5d/8QtevZo//JCrq92v9F138bZtQaz0bW1thYWFni/FsKWrq6tr/fr10dHRRHR3UpJ982bu7Q1gdKuVi4sbFi0iopSUlMrKypG7R5vNZrFY1GWrwWAwmUwXLlzwa3C1BMTHMxGPG8dmM99qWVH7nORkJmJN46IiR1ubz+FHLgF+zerb/MpdLS133323erKioqIzZ84E8WRKTU1NVlbWsHm7XK4333xz8uTJ6pV+4oknTp06FcTg9ubmhQsXqkEWLFgw7LxfU1Mza9Ys9dGcnJza2trARu/qYpPJHfTUqfz22zc5pr6e8/Pdb4b77+eqKj9P2SOXrlttIM+dO2c0Gn+/aJH7fVVWxj63mi4XV1a6C4uN/evvftfT0+P1E+0qLi5W58YJEyaYzWabzebl+Lq6ur+tWuX+rFes4C+/9DEfZr56lS0WnjiRo6KW33efyWTq7Oy86YHel4CABHCp2tvb63k9oqOj1aoZ0JO1t7cbjUY17+zs7CNHjgw7YGBgoKysLCEhgYhezctjo/H6SdCnq1fZbObo6G2PPnqrpYuZnU5nVVWV531VUFDgz/tqyOHgV1+9vnRt3nzLpUvZv5+zstTLP1RQ8Mknn3gfv7q6eurUqQEtXa5jx3jePHdhM2bwO+/c8tDGRp4/333kggXs9xbliy++8JwS09LSysvLR24eLly4YDQaNU2Ljo5uycvzNo2b6uho+s1v1FYzMTFx69atAzdcxY5+9zJMwHdmzp8/bzKZ1PzuvPNOi8Uy4MdVtuo4Li5OrRYWi8XLte+lS5fMJSUDEyYwEU+YwKWlfPWqt9FdLt61i1NSmIgNhqslJT7fh319fRaL5Y477iCiqKgok8nkpbC6urrs7Oz9ublMxIWF7MeZl5nZ4eDyck5JqV20iIgKCwtbW1tHHjVs6Rq5BHjjcnFVFU+b5k65oIBPnmRmHhhgtQOx27m4mA0GJuLvfY937w7i6vCjjz6aN2+emuGMGTPeuRa0w+EoKytT255x48aZzeagL4pOnz7tufrMyMhQS1UQS4BPQd6IPHHiRF5enprfAw884P0q9tChQ2r3ol719vZ2v57j3//moiL3ziE1lcvL+abv7JYWLihwv96PPMKB3HC8dOmS55QdFxc38pTtWbqI6PFHH7357sW7np6XzWZ1lRITE/Pcc89dvnxZfWRgYMBisailKz4+3svuxYfBQS4v56QkJuI//Yn//nf+8Y/ZbObCQv7qK547lw0GLi7mAE/FN1JXsWrrTESLFy/esmVLdna25zUdzebW49133505c6YaU33FKPB7L96N6r57TU2NZ35z5849duzYsANu3L1kZWXV1NQE/BxHjvCcOe6aH3yQz53jc+f4tde4spL7+njPHvfSlZzMO3cGd2OrpaXFc8pOT09XV7E3Ll1q53bV+xnGq46ODpPJpO5wJyYmWiyWt956a+QFzKhcvsxmM9tsnJfn/jocPcolJXzqlP+7F+9sNttLL72kTonqc5k2bdqBAwd0GVxxOp3q1pBaBSIjI/W9Az7abzOpq1h1B1ddxba1tfGI3YvZbPZnz3NznlN2VhafPcvLlnFDA//jH/z973NnJyclsdHIXV2j/EQOHTrkuYpNT0/3bO5vtQkJwmeffbZ48WK6QcC7F5+6unjlSvdjq5V/+EM9B2dm5s7Oztzc3PHjxz///PM63NIdITc3l4iKi4tVUfoOrs93Va1Wa0lJied7Ijk5ORkZGZ6ly987Wd719/N//sOvvHJ9R7F+PZ88yV7vMAREnbIzMjI0TYuJiUlPT6+srNRrcI8DBw5kZmbGxMRs3LhR/2/eOZ2cn+9+XF/PGzboPP41wS9evjz22GNEdPToUXUC0ev7MIqeP0TQ3t7uuYoloszMzGB2L95t3swffuh+XFoa0Dcp/NTV1bV69ep169Z5v/U2Gg6H45tvvrlNg/P27bx2LVdUcGGhXzcExxh1TVhbW6tWT31PIPr/zMzevXvnzJnz9NNP35afOzh4kF94gZl5aIiXL+drl33wLR0dfOIE9/WFeh7BUPu9mpoatRPuDej7aL7o/wPAK1euXLlype7Dui1ZQvX1tGYN9ffT2rV07SdJ4FvS0sL0R5Hpht/V8P83UP0X6r8RGYTf/jbUM4DbyPOLp/7/BmoAg+s4FsDorZo8+fF589I1zfLII9G9vTHIHb7Dnu7spOPHyWab9a9/0fnz+v6xrVD/4Q2AYdTfYhkacv8NIuQO32Weyj3d6we5wxiD1R0EweoOgngqVw+wusN3mWd1Vw9wIxK+y6ZPp4ICSkujJUsoPZ0SEnQcW2P1x6YBxo7Dh2nfPjIY6Fe/ounTdRwYqzuMMS0t9NprtGcP9fbSj35E1dUUF6fX2Ni7wxjz/vv0s59RVBRNmkSLF1N9vY5jI3cYYzSNPBts9X/e1Q9yhzFm2TKqrCSHg7q7qbaWcnJ0HBuXqjD2qEvVyEhau5au/Q0LXSB3EASbGRAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0E+R8OYdUeDeb1uwAAAABJRU5ErkJggg==)
Find more compounds similar to Propanoic acid, 3-ethoxy-, ethyl ester.
Mixtures
- Propanoic acid, 3-ethoxy-, ethyl ester + 2-Propenoic acid, 2-methyl-
- Benzyl methacrylate + Propanoic acid, 3-ethoxy-, ethyl ester
- Propanoic acid, 3-ethoxy-, ethyl ester + 2-Hydroxyethyl methacrylate
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Density and Viscosity for Ethyl 3-Ethoxypropionate + Methacrylic Acid, + Benzyl Methacrylate, and + 2-Hydroxyethyl Methacrylate
- Joback Method
- McGowan Method
- NIST Webbook
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