- Name
- 1,3-Propanediol
- InChI
- InChI=1S/C3H8O2/c4-2-1-3-5/h4-5H,1-3H2
- InChI Key
- YPFDHNVEDLHUCE-UHFFFAOYSA-N
- Formula
- C3H8O2
- SMILES
- OCCCO
- Mol. Weight (g/mol)
- 76.09
- CAS
- 504-63-2
- Name
- Propylamine
- InChI
- InChI=1S/C3H9N/c1-2-3-4/h2-4H2,1H3
- InChI Key
- WGYKZJWCGVVSQN-UHFFFAOYSA-N
- Formula
- C3H9N
- SMILES
- CCCN
- Mol. Weight (g/mol)
- 59.11
- CAS
- 107-10-8
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Datasets
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1,3-Propanediol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0044 | -0.0965 |
| 0.0088 | -0.1908 |
| 0.0132 | -0.2893 |
| 0.0177 | -0.3959 |
| 0.0220 | -0.4861 |
| 0.0263 | -0.5850 |
| 0.0305 | -0.6656 |
| 0.0347 | -0.7542 |
| 0.0389 | -0.8429 |
| 0.0430 | -0.9305 |
| 0.0471 | -1.0151 |
| 0.0512 | -1.1005 |
| 0.0552 | -1.1835 |
| 0.0592 | -1.2644 |
| 0.0632 | -1.3457 |
| 0.0671 | -1.4265 |
| 0.0710 | -1.4954 |
| 0.0748 | -1.5734 |
| 0.0787 | -1.6469 |
| 0.0825 | -1.7198 |
| 0.0862 | -1.7882 |
| 0.0900 | -1.8598 |
| 0.0937 | -1.93 |
| 0.0974 | -2.0 |
| 0.1010 | -2.0689 |
| 0.1046 | -2.1359 |
| 0.1082 | -2.2017 |
| 0.1118 | -2.2632 |
| 0.1153 | -2.326 |
| 0.1188 | -2.3902 |
| 0.1223 | -2.4495 |
| 0.1257 | -2.5052 |
| 0.1292 | -2.5652 |
| 0.1359 | -2.6805 |
| 0.1491 | -2.8903 |
| 0.1556 | -2.9927 |
| 0.1620 | -3.092 |
| 0.1682 | -3.1874 |
| 0.1744 | -3.2786 |
| 0.1805 | -3.3659 |
| 0.1865 | -3.4502 |
| 0.1924 | -3.5302 |
| 0.1982 | -3.6079 |
| 0.2096 | -3.7612 |
| 0.2124 | -3.7966 |
| 0.2152 | -3.8298 |
| 0.2180 | -3.8682 |
| 0.2208 | -3.8991 |
| 0.2263 | -3.9647 |
| 0.2274 | -3.9793 |
| 0.2319 | -4.0275 |
| 0.2342 | -4.0549 |
| 0.2414 | -4.136 |
| 0.2464 | -4.1929 |
| 0.2516 | -4.2489 |
| 0.2571 | -4.3053 |
| 0.2629 | -4.3625 |
| 0.2719 | -4.4498 |
| 0.2851 | -4.5772 |
| 0.2996 | -4.6984 |
| 0.3074 | -4.76 |
| 0.3156 | -4.8144 |
| 0.3242 | -4.8783 |
| 0.3334 | -4.9352 |
| 0.3431 | -4.9944 |
| 0.3534 | -5.0504 |
| 0.3700 | -5.1213 |
| 0.3759 | -5.1471 |
| 0.3820 | -5.1684 |
| 0.3883 | -5.1884 |
| 0.3948 | -5.2168 |
| 0.4015 | -5.2238 |
| 0.4156 | -5.2502 |
| 0.4280 | -5.2683 |
| 0.4371 | -5.275 |
| 0.4466 | -5.2717 |
| 0.4565 | -5.272 |
| 0.4616 | -5.2721 |
| 0.4668 | -5.2647 |
| 0.4776 | -5.2518 |
| 0.4832 | -5.2426 |
| 0.4948 | -5.2132 |
| 0.5009 | -5.1972 |
| 0.5070 | -5.1824 |
| 0.5198 | -5.1359 |
| 0.5264 | -5.1119 |
| 0.5367 | -5.0711 |
| 0.5403 | -5.051 |
| 0.5438 | -5.0368 |
| 0.5474 | -5.0169 |
| 0.5511 | -4.9963 |
| 0.5548 | -4.9756 |
| 0.5585 | -4.9573 |
| 0.5662 | -4.9151 |
| 0.5701 | -4.8916 |
| 0.5741 | -4.8725 |
| 0.5781 | -4.8448 |
| 0.5906 | -4.7669 |
| 0.5991 | -4.7051 |
| 0.6080 | -4.64 |
| 0.6171 | -4.5781 |
| 0.6265 | -4.5034 |
| 0.6361 | -4.4234 |
| 0.6411 | -4.3837 |
| 0.6495 | -4.3149 |
| 0.6564 | -4.2531 |
| 0.6600 | -4.2211 |
| 0.6636 | -4.1923 |
| 0.6672 | -4.1616 |
| 0.6708 | -4.1286 |
| 0.6783 | -4.0589 |
| 0.6821 | -4.0233 |
| 0.6859 | -3.9858 |
| 0.6898 | -3.9521 |
| 0.6937 | -3.9177 |
| 0.6976 | -3.8821 |
| 0.7057 | -3.8015 |
| 0.7139 | -3.7198 |
| 0.7224 | -3.6318 |
| 0.7310 | -3.5378 |
| 0.7443 | -3.3947 |
| 0.7535 | -3.2934 |
| 0.7677 | -3.1338 |
| 0.7726 | -3.0782 |
| 0.7978 | -2.7784 |
| 0.8083 | -2.6522 |
| 0.8137 | -2.5817 |
| 0.8247 | -2.4428 |
| 0.8303 | -2.3722 |
| 0.8359 | -2.3029 |
| 0.8417 | -2.2277 |
| 0.8475 | -2.1547 |
| 0.8534 | -2.0783 |
| 0.8594 | -1.9998 |
| 0.8655 | -1.9193 |
| 0.8717 | -1.8389 |
| 0.8780 | -1.7519 |
| 0.8843 | -1.6685 |
| 0.8869 | -1.6296 |
| 0.8894 | -1.5934 |
| 0.8920 | -1.5596 |
| 0.8946 | -1.5234 |
| 0.8973 | -1.4873 |
| 0.8999 | -1.4517 |
| 0.9026 | -1.4159 |
| 0.9052 | -1.3773 |
| 0.9079 | -1.3392 |
| 0.9134 | -1.2655 |
| 0.9161 | -1.2257 |
| 0.9188 | -1.1895 |
| 0.9216 | -1.149 |
| 0.9244 | -1.1111 |
| 0.9272 | -1.0725 |
| 0.9300 | -1.0335 |
| 0.9329 | -0.9940 |
| 0.9357 | -0.9543 |
| 0.9386 | -0.9146 |
| 0.9415 | -0.8741 |
| 0.9444 | -0.8331 |
| 0.9473 | -0.7887 |
| 0.9503 | -0.7452 |
| 0.9532 | -0.7019 |
| 0.9562 | -0.6605 |
| 0.9592 | -0.6159 |
| 0.9622 | -0.5708 |
| 0.9666 | -0.4989 |
| 0.9695 | -0.4590 |
| 0.9725 | -0.4124 |
| 0.9755 | -0.3698 |
| 0.9785 | -0.3257 |
| 0.9815 | -0.2790 |
| 0.9845 | -0.2348 |
| 0.9876 | -0.1860 |
| 0.9907 | -0.1408 |
| 0.9935 | -0.1020 |
| 0.9938 | -0.0949 |
| 0.9967 | -0.0515 |
| 0.9969 | -0.0474 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1,3-Propanediol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0044 | -0.0965 |
| 0.0088 | -0.1908 |
| 0.0132 | -0.2893 |
| 0.0177 | -0.3959 |
| 0.0220 | -0.4861 |
| 0.0263 | -0.5850 |
| 0.0305 | -0.6656 |
| 0.0347 | -0.7542 |
| 0.0389 | -0.8429 |
| 0.0430 | -0.9305 |
| 0.0471 | -1.0151 |
| 0.0512 | -1.1005 |
| 0.0552 | -1.1835 |
| 0.0592 | -1.2644 |
| 0.0632 | -1.3457 |
| 0.0671 | -1.4265 |
| 0.0710 | -1.4954 |
| 0.0748 | -1.5734 |
| 0.0787 | -1.6469 |
| 0.0825 | -1.7198 |
| 0.0862 | -1.7882 |
| 0.0900 | -1.8598 |
| 0.0937 | -1.93 |
| 0.0974 | -2.0 |
| 0.1010 | -2.0689 |
| 0.1046 | -2.1359 |
| 0.1082 | -2.2017 |
| 0.1118 | -2.2632 |
| 0.1153 | -2.326 |
| 0.1188 | -2.3902 |
| 0.1223 | -2.4495 |
| 0.1257 | -2.5052 |
| 0.1292 | -2.5652 |
| 0.1359 | -2.6805 |
| 0.1491 | -2.8903 |
| 0.1556 | -2.9927 |
| 0.1620 | -3.092 |
| 0.1682 | -3.1874 |
| 0.1744 | -3.2786 |
| 0.1805 | -3.3659 |
| 0.1865 | -3.4502 |
| 0.1924 | -3.5302 |
| 0.1982 | -3.6079 |
| 0.2096 | -3.7612 |
| 0.2124 | -3.7966 |
| 0.2152 | -3.8298 |
| 0.2180 | -3.8682 |
| 0.2208 | -3.8991 |
| 0.2263 | -3.9647 |
| 0.2274 | -3.9793 |
| 0.2319 | -4.0275 |
| 0.2342 | -4.0549 |
| 0.2414 | -4.136 |
| 0.2464 | -4.1929 |
| 0.2516 | -4.2489 |
| 0.2571 | -4.3053 |
| 0.2629 | -4.3625 |
| 0.2719 | -4.4498 |
| 0.2851 | -4.5772 |
| 0.2996 | -4.6984 |
| 0.3074 | -4.76 |
| 0.3156 | -4.8144 |
| 0.3242 | -4.8783 |
| 0.3334 | -4.9352 |
| 0.3431 | -4.9944 |
| 0.3534 | -5.0504 |
| 0.3700 | -5.1213 |
| 0.3759 | -5.1471 |
| 0.3820 | -5.1684 |
| 0.3883 | -5.1884 |
| 0.3948 | -5.2168 |
| 0.4015 | -5.2238 |
| 0.4156 | -5.2502 |
| 0.4280 | -5.2683 |
| 0.4371 | -5.275 |
| 0.4466 | -5.2717 |
| 0.4565 | -5.272 |
| 0.4616 | -5.2721 |
| 0.4668 | -5.2647 |
| 0.4776 | -5.2518 |
| 0.4832 | -5.2426 |
| 0.4948 | -5.2132 |
| 0.5009 | -5.1972 |
| 0.5070 | -5.1824 |
| 0.5198 | -5.1359 |
| 0.5264 | -5.1119 |
| 0.5367 | -5.0711 |
| 0.5403 | -5.051 |
| 0.5438 | -5.0368 |
| 0.5474 | -5.0169 |
| 0.5511 | -4.9963 |
| 0.5548 | -4.9756 |
| 0.5585 | -4.9573 |
| 0.5662 | -4.9151 |
| 0.5701 | -4.8916 |
| 0.5741 | -4.8725 |
| 0.5781 | -4.8448 |
| 0.5906 | -4.7669 |
| 0.5991 | -4.7051 |
| 0.6080 | -4.64 |
| 0.6171 | -4.5781 |
| 0.6265 | -4.5034 |
| 0.6361 | -4.4234 |
| 0.6411 | -4.3837 |
| 0.6495 | -4.3149 |
| 0.6564 | -4.2531 |
| 0.6600 | -4.2211 |
| 0.6636 | -4.1923 |
| 0.6672 | -4.1616 |
| 0.6708 | -4.1286 |
| 0.6783 | -4.0589 |
| 0.6821 | -4.0233 |
| 0.6859 | -3.9858 |
| 0.6898 | -3.9521 |
| 0.6937 | -3.9177 |
| 0.6976 | -3.8821 |
| 0.7057 | -3.8015 |
| 0.7139 | -3.7198 |
| 0.7224 | -3.6318 |
| 0.7310 | -3.5378 |
| 0.7443 | -3.3947 |
| 0.7535 | -3.2934 |
| 0.7677 | -3.1338 |
| 0.7726 | -3.0782 |
| 0.7978 | -2.7784 |
| 0.8083 | -2.6522 |
| 0.8137 | -2.5817 |
| 0.8247 | -2.4428 |
| 0.8303 | -2.3722 |
| 0.8359 | -2.3029 |
| 0.8417 | -2.2277 |
| 0.8475 | -2.1547 |
| 0.8534 | -2.0783 |
| 0.8594 | -1.9998 |
| 0.8655 | -1.9193 |
| 0.8717 | -1.8389 |
| 0.8780 | -1.7519 |
| 0.8843 | -1.6685 |
| 0.8869 | -1.6296 |
| 0.8894 | -1.5934 |
| 0.8920 | -1.5596 |
| 0.8946 | -1.5234 |
| 0.8973 | -1.4873 |
| 0.8999 | -1.4517 |
| 0.9026 | -1.4159 |
| 0.9052 | -1.3773 |
| 0.9079 | -1.3392 |
| 0.9134 | -1.2655 |
| 0.9161 | -1.2257 |
| 0.9188 | -1.1895 |
| 0.9216 | -1.149 |
| 0.9244 | -1.1111 |
| 0.9272 | -1.0725 |
| 0.9300 | -1.0335 |
| 0.9329 | -0.9940 |
| 0.9357 | -0.9543 |
| 0.9386 | -0.9146 |
| 0.9415 | -0.8741 |
| 0.9444 | -0.8331 |
| 0.9473 | -0.7887 |
| 0.9503 | -0.7452 |
| 0.9532 | -0.7019 |
| 0.9562 | -0.6605 |
| 0.9592 | -0.6159 |
| 0.9622 | -0.5708 |
| 0.9666 | -0.4989 |
| 0.9695 | -0.4590 |
| 0.9725 | -0.4124 |
| 0.9755 | -0.3698 |
| 0.9785 | -0.3257 |
| 0.9815 | -0.2790 |
| 0.9845 | -0.2348 |
| 0.9876 | -0.1860 |
| 0.9907 | -0.1408 |
| 0.9935 | -0.1020 |
| 0.9938 | -0.0949 |
| 0.9967 | -0.0515 |
| 0.9969 | -0.0474 |