- Name
- Diethyl malonate
- InChI
- InChI=1S/C7H12O4/c1-3-10-6(8)5-7(9)11-4-2/h3-5H2,1-2H3
- InChI Key
- IYXGSMUGOJNHAZ-UHFFFAOYSA-N
- Formula
- C7H12O4
- SMILES
- CCOC(=O)CC(=O)OCC
- Mol. Weight (g/mol)
- 160.17
- CAS
- 105-53-3
- Name
- 1-Pentanol
- InChI
- InChI=1S/C5H12O/c1-2-3-4-5-6/h6H,2-5H2,1H3
- InChI Key
- AMQJEAYHLZJPGS-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- CCCCCO
- Mol. Weight (g/mol)
- 88.15
- CAS
- 71-41-0
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Datasets
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 288.15 | 0.0583 | 0.6420 |
| 288.15 | 0.1007 | 0.9850 |
| 288.15 | 0.1478 | 1.299 |
| 288.15 | 0.2000 | 1.561 |
| 288.15 | 0.2474 | 1.759 |
| 288.15 | 0.3001 | 1.934 |
| 288.15 | 0.3474 | 2.044 |
| 288.15 | 0.4003 | 2.142 |
| 288.15 | 0.4472 | 2.177 |
| 288.15 | 0.4997 | 2.211 |
| 288.15 | 0.5500 | 2.209 |
| 288.15 | 0.5975 | 2.159 |
| 288.15 | 0.6466 | 2.069 |
| 288.15 | 0.6973 | 1.947 |
| 288.15 | 0.7497 | 1.757 |
| 288.15 | 0.7988 | 1.552 |
| 288.15 | 0.8494 | 1.257 |
| 288.15 | 0.9017 | 0.8890 |
| 288.15 | 0.9501 | 0.4600 |
| 298.15 | 0.0494 | 0.6090 |
| 298.15 | 0.1007 | 1.079 |
| 298.15 | 0.1478 | 1.414 |
| 298.15 | 0.2000 | 1.729 |
| 298.15 | 0.2474 | 1.944 |
| 298.15 | 0.3001 | 2.156 |
| 298.15 | 0.3474 | 2.271 |
| 298.15 | 0.4003 | 2.39 |
| 298.15 | 0.4472 | 2.445 |
| 298.15 | 0.4997 | 2.467 |
| 298.15 | 0.5500 | 2.433 |
| 298.15 | 0.5975 | 2.374 |
| 298.15 | 0.6466 | 2.272 |
| 298.15 | 0.6973 | 2.12 |
| 298.15 | 0.7497 | 1.913 |
| 298.15 | 0.7988 | 1.666 |
| 298.15 | 0.8494 | 1.338 |
| 298.15 | 0.9017 | 0.9320 |
| 298.15 | 0.9501 | 0.5030 |
| 313.15 | 0.0583 | 0.7490 |
| 313.15 | 0.1007 | 1.181 |
| 313.15 | 0.1478 | 1.619 |
| 313.15 | 0.2000 | 1.918 |
| 313.15 | 0.2474 | 2.174 |
| 313.15 | 0.3001 | 2.424 |
| 313.15 | 0.3474 | 2.57 |
| 313.15 | 0.4003 | 2.673 |
| 313.15 | 0.4472 | 2.705 |
| 313.15 | 0.4997 | 2.706 |
| 313.15 | 0.5500 | 2.68 |
| 313.15 | 0.5975 | 2.598 |
| 313.15 | 0.6466 | 2.471 |
| 313.15 | 0.6973 | 2.279 |
| 313.15 | 0.7497 | 2.032 |
| 313.15 | 0.7988 | 1.751 |
| 313.15 | 0.8494 | 1.39 |
| 313.15 | 0.9017 | 0.9450 |
| 313.15 | 0.9501 | 0.5080 |
| 328.15 | 0.0583 | 0.7160 |
| 328.15 | 0.1007 | 1.221 |
| 328.15 | 0.1478 | 1.636 |
| 328.15 | 0.2000 | 2.033 |
| 328.15 | 0.2474 | 2.289 |
| 328.15 | 0.3001 | 2.53 |
| 328.15 | 0.3474 | 2.688 |
| 328.15 | 0.4003 | 2.789 |
| 328.15 | 0.4472 | 2.842 |
| 328.15 | 0.4997 | 2.853 |
| 328.15 | 0.5500 | 2.799 |
| 328.15 | 0.5975 | 2.701 |
| 328.15 | 0.6466 | 2.561 |
| 328.15 | 0.6973 | 2.347 |
| 328.15 | 0.7497 | 2.081 |
| 328.15 | 0.7988 | 1.772 |
| 328.15 | 0.8494 | 1.398 |
| 328.15 | 0.9017 | 0.9700 |
| 328.15 | 0.9501 | 0.5070 |
| 338.15 | 0.0583 | 0.7760 |
| 338.15 | 0.1007 | 1.229 |
| 338.15 | 0.1478 | 1.646 |
| 338.15 | 0.2000 | 2.049 |
| 338.15 | 0.2474 | 2.303 |
| 338.15 | 0.3001 | 2.575 |
| 338.15 | 0.3474 | 2.712 |
| 338.15 | 0.4003 | 2.806 |
| 338.15 | 0.4472 | 2.845 |
| 338.15 | 0.4997 | 2.856 |
| 338.15 | 0.5500 | 2.8 |
| 338.15 | 0.5975 | 2.694 |
| 338.15 | 0.6466 | 2.499 |
| 338.15 | 0.6973 | 2.33 |
| 338.15 | 0.7497 | 2.058 |
| 338.15 | 0.7988 | 1.765 |
| 338.15 | 0.8494 | 1.386 |
| 338.15 | 0.9017 | 0.9360 |
| 338.15 | 0.9501 | 0.4780 |
| 348.15 | 0.0583 | 0.8140 |
| 348.15 | 0.1007 | 1.259 |
| 348.15 | 0.1478 | 1.668 |
| 348.15 | 0.2000 | 2.05 |
| 348.15 | 0.2474 | 2.329 |
| 348.15 | 0.3001 | 2.539 |
| 348.15 | 0.3474 | 2.695 |
| 348.15 | 0.4003 | 2.83 |
| 348.15 | 0.4472 | 2.852 |
| 348.15 | 0.4997 | 2.837 |
| 348.15 | 0.5500 | 2.785 |
| 348.15 | 0.5975 | 2.68 |
| 348.15 | 0.6466 | 2.507 |
| 348.15 | 0.6973 | 2.3 |
| 348.15 | 0.7497 | 2.019 |
| 348.15 | 0.7988 | 1.703 |
| 348.15 | 0.8494 | 1.317 |
| 348.15 | 0.9017 | 0.9080 |
| 348.15 | 0.9501 | 0.4580 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 288.15 | 0.0583 | 0.6420 |
| 288.15 | 0.1007 | 0.9850 |
| 288.15 | 0.1478 | 1.299 |
| 288.15 | 0.2000 | 1.561 |
| 288.15 | 0.2474 | 1.759 |
| 288.15 | 0.3001 | 1.934 |
| 288.15 | 0.3474 | 2.044 |
| 288.15 | 0.4003 | 2.142 |
| 288.15 | 0.4472 | 2.177 |
| 288.15 | 0.4997 | 2.211 |
| 288.15 | 0.5500 | 2.209 |
| 288.15 | 0.5975 | 2.159 |
| 288.15 | 0.6466 | 2.069 |
| 288.15 | 0.6973 | 1.947 |
| 288.15 | 0.7497 | 1.757 |
| 288.15 | 0.7988 | 1.552 |
| 288.15 | 0.8494 | 1.257 |
| 288.15 | 0.9017 | 0.8890 |
| 288.15 | 0.9501 | 0.4600 |
| 298.15 | 0.0494 | 0.6090 |
| 298.15 | 0.1007 | 1.079 |
| 298.15 | 0.1478 | 1.414 |
| 298.15 | 0.2000 | 1.729 |
| 298.15 | 0.2474 | 1.944 |
| 298.15 | 0.3001 | 2.156 |
| 298.15 | 0.3474 | 2.271 |
| 298.15 | 0.4003 | 2.39 |
| 298.15 | 0.4472 | 2.445 |
| 298.15 | 0.4997 | 2.467 |
| 298.15 | 0.5500 | 2.433 |
| 298.15 | 0.5975 | 2.374 |
| 298.15 | 0.6466 | 2.272 |
| 298.15 | 0.6973 | 2.12 |
| 298.15 | 0.7497 | 1.913 |
| 298.15 | 0.7988 | 1.666 |
| 298.15 | 0.8494 | 1.338 |
| 298.15 | 0.9017 | 0.9320 |
| 298.15 | 0.9501 | 0.5030 |
| 313.15 | 0.0583 | 0.7490 |
| 313.15 | 0.1007 | 1.181 |
| 313.15 | 0.1478 | 1.619 |
| 313.15 | 0.2000 | 1.918 |
| 313.15 | 0.2474 | 2.174 |
| 313.15 | 0.3001 | 2.424 |
| 313.15 | 0.3474 | 2.57 |
| 313.15 | 0.4003 | 2.673 |
| 313.15 | 0.4472 | 2.705 |
| 313.15 | 0.4997 | 2.706 |
| 313.15 | 0.5500 | 2.68 |
| 313.15 | 0.5975 | 2.598 |
| 313.15 | 0.6466 | 2.471 |
| 313.15 | 0.6973 | 2.279 |
| 313.15 | 0.7497 | 2.032 |
| 313.15 | 0.7988 | 1.751 |
| 313.15 | 0.8494 | 1.39 |
| 313.15 | 0.9017 | 0.9450 |
| 313.15 | 0.9501 | 0.5080 |
| 328.15 | 0.0583 | 0.7160 |
| 328.15 | 0.1007 | 1.221 |
| 328.15 | 0.1478 | 1.636 |
| 328.15 | 0.2000 | 2.033 |
| 328.15 | 0.2474 | 2.289 |
| 328.15 | 0.3001 | 2.53 |
| 328.15 | 0.3474 | 2.688 |
| 328.15 | 0.4003 | 2.789 |
| 328.15 | 0.4472 | 2.842 |
| 328.15 | 0.4997 | 2.853 |
| 328.15 | 0.5500 | 2.799 |
| 328.15 | 0.5975 | 2.701 |
| 328.15 | 0.6466 | 2.561 |
| 328.15 | 0.6973 | 2.347 |
| 328.15 | 0.7497 | 2.081 |
| 328.15 | 0.7988 | 1.772 |
| 328.15 | 0.8494 | 1.398 |
| 328.15 | 0.9017 | 0.9700 |
| 328.15 | 0.9501 | 0.5070 |
| 338.15 | 0.0583 | 0.7760 |
| 338.15 | 0.1007 | 1.229 |
| 338.15 | 0.1478 | 1.646 |
| 338.15 | 0.2000 | 2.049 |
| 338.15 | 0.2474 | 2.303 |
| 338.15 | 0.3001 | 2.575 |
| 338.15 | 0.3474 | 2.712 |
| 338.15 | 0.4003 | 2.806 |
| 338.15 | 0.4472 | 2.845 |
| 338.15 | 0.4997 | 2.856 |
| 338.15 | 0.5500 | 2.8 |
| 338.15 | 0.5975 | 2.694 |
| 338.15 | 0.6466 | 2.499 |
| 338.15 | 0.6973 | 2.33 |
| 338.15 | 0.7497 | 2.058 |
| 338.15 | 0.7988 | 1.765 |
| 338.15 | 0.8494 | 1.386 |
| 338.15 | 0.9017 | 0.9360 |
| 338.15 | 0.9501 | 0.4780 |
| 348.15 | 0.0583 | 0.8140 |
| 348.15 | 0.1007 | 1.259 |
| 348.15 | 0.1478 | 1.668 |
| 348.15 | 0.2000 | 2.05 |
| 348.15 | 0.2474 | 2.329 |
| 348.15 | 0.3001 | 2.539 |
| 348.15 | 0.3474 | 2.695 |
| 348.15 | 0.4003 | 2.83 |
| 348.15 | 0.4472 | 2.852 |
| 348.15 | 0.4997 | 2.837 |
| 348.15 | 0.5500 | 2.785 |
| 348.15 | 0.5975 | 2.68 |
| 348.15 | 0.6466 | 2.507 |
| 348.15 | 0.6973 | 2.3 |
| 348.15 | 0.7497 | 2.019 |
| 348.15 | 0.7988 | 1.703 |
| 348.15 | 0.8494 | 1.317 |
| 348.15 | 0.9017 | 0.9080 |
| 348.15 | 0.9501 | 0.4580 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 818.801 |
| 288.15 | 0.0999 | 849.562 |
| 288.15 | 0.1998 | 878.757 |
| 288.15 | 0.2999 | 906.036 |
| 288.15 | 0.3498 | 919.092 |
| 288.15 | 0.3997 | 931.801 |
| 288.15 | 0.4499 | 944.204 |
| 288.15 | 0.4999 | 956.145 |
| 288.15 | 0.5501 | 967.903 |
| 288.15 | 0.5990 | 978.962 |
| 288.15 | 0.6500 | 990.137 |
| 288.15 | 0.6997 | 1000.807 |
| 288.15 | 0.7997 | 1021.522 |
| 288.15 | 0.9000 | 1041.367 |
| 288.15 | 1.0000 | 1060.326 |
| 298.15 | 0.0000 | 811.465 |
| 298.15 | 0.0999 | 841.661 |
| 298.15 | 0.1998 | 870.343 |
| 298.15 | 0.2999 | 897.187 |
| 298.15 | 0.3498 | 910.054 |
| 298.15 | 0.3997 | 922.576 |
| 298.15 | 0.4499 | 934.797 |
| 298.15 | 0.4999 | 946.568 |
| 298.15 | 0.5501 | 958.185 |
| 298.15 | 0.5990 | 969.118 |
| 298.15 | 0.6500 | 980.151 |
| 298.15 | 0.6997 | 990.684 |
| 298.15 | 0.7997 | 1011.18 |
| 298.15 | 0.9000 | 1030.84 |
| 298.15 | 1.0000 | 1049.603 |
| 313.15 | 0.0000 | 800.264 |
| 313.15 | 0.0999 | 829.624 |
| 313.15 | 0.1998 | 857.553 |
| 313.15 | 0.2999 | 883.774 |
| 313.15 | 0.3498 | 896.347 |
| 313.15 | 0.3997 | 908.607 |
| 313.15 | 0.4499 | 920.565 |
| 313.15 | 0.4999 | 932.101 |
| 313.15 | 0.5501 | 943.506 |
| 313.15 | 0.5990 | 954.233 |
| 313.15 | 0.6500 | 965.074 |
| 313.15 | 0.6997 | 975.442 |
| 313.15 | 0.7997 | 995.601 |
| 313.15 | 0.9000 | 1014.995 |
| 313.15 | 1.0000 | 1033.498 |
| 328.15 | 0.0000 | 788.737 |
| 328.15 | 0.0999 | 817.296 |
| 328.15 | 0.1998 | 844.519 |
| 328.15 | 0.2999 | 870.127 |
| 328.15 | 0.3498 | 882.426 |
| 328.15 | 0.3997 | 894.428 |
| 328.15 | 0.4499 | 906.141 |
| 328.15 | 0.4999 | 917.475 |
| 328.15 | 0.5501 | 928.648 |
| 328.15 | 0.5990 | 939.199 |
| 328.15 | 0.6500 | 949.864 |
| 328.15 | 0.6997 | 960.07 |
| 328.15 | 0.7997 | 979.945 |
| 328.15 | 0.9000 | 999.065 |
| 328.15 | 1.0000 | 1017.336 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 818.801 |
| 288.15 | 0.0999 | 849.562 |
| 288.15 | 0.1998 | 878.757 |
| 288.15 | 0.2999 | 906.036 |
| 288.15 | 0.3498 | 919.092 |
| 288.15 | 0.3997 | 931.801 |
| 288.15 | 0.4499 | 944.204 |
| 288.15 | 0.4999 | 956.145 |
| 288.15 | 0.5501 | 967.903 |
| 288.15 | 0.5990 | 978.962 |
| 288.15 | 0.6500 | 990.137 |
| 288.15 | 0.6997 | 1000.807 |
| 288.15 | 0.7997 | 1021.522 |
| 288.15 | 0.9000 | 1041.367 |
| 288.15 | 1.0000 | 1060.326 |
| 298.15 | 0.0000 | 811.465 |
| 298.15 | 0.0999 | 841.661 |
| 298.15 | 0.1998 | 870.343 |
| 298.15 | 0.2999 | 897.187 |
| 298.15 | 0.3498 | 910.054 |
| 298.15 | 0.3997 | 922.576 |
| 298.15 | 0.4499 | 934.797 |
| 298.15 | 0.4999 | 946.568 |
| 298.15 | 0.5501 | 958.185 |
| 298.15 | 0.5990 | 969.118 |
| 298.15 | 0.6500 | 980.151 |
| 298.15 | 0.6997 | 990.684 |
| 298.15 | 0.7997 | 1011.18 |
| 298.15 | 0.9000 | 1030.84 |
| 298.15 | 1.0000 | 1049.603 |
| 313.15 | 0.0000 | 800.264 |
| 313.15 | 0.0999 | 829.624 |
| 313.15 | 0.1998 | 857.553 |
| 313.15 | 0.2999 | 883.774 |
| 313.15 | 0.3498 | 896.347 |
| 313.15 | 0.3997 | 908.607 |
| 313.15 | 0.4499 | 920.565 |
| 313.15 | 0.4999 | 932.101 |
| 313.15 | 0.5501 | 943.506 |
| 313.15 | 0.5990 | 954.233 |
| 313.15 | 0.6500 | 965.074 |
| 313.15 | 0.6997 | 975.442 |
| 313.15 | 0.7997 | 995.601 |
| 313.15 | 0.9000 | 1014.995 |
| 313.15 | 1.0000 | 1033.498 |
| 328.15 | 0.0000 | 788.737 |
| 328.15 | 0.0999 | 817.296 |
| 328.15 | 0.1998 | 844.519 |
| 328.15 | 0.2999 | 870.127 |
| 328.15 | 0.3498 | 882.426 |
| 328.15 | 0.3997 | 894.428 |
| 328.15 | 0.4499 | 906.141 |
| 328.15 | 0.4999 | 917.475 |
| 328.15 | 0.5501 | 928.648 |
| 328.15 | 0.5990 | 939.199 |
| 328.15 | 0.6500 | 949.864 |
| 328.15 | 0.6997 | 960.07 |
| 328.15 | 0.7997 | 979.945 |
| 328.15 | 0.9000 | 999.065 |
| 328.15 | 1.0000 | 1017.336 |
Sources
- Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
- Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K