- Name
- Propanedioic acid
- InChI
- InChI=1S/C3H4O4/c4-2(5)1-3(6)7/h1H2,(H,4,5)(H,6,7)
- InChI Key
- OFOBLEOULBTSOW-UHFFFAOYSA-N
- Formula
- C3H4O4
- SMILES
- O=C(O)CC(=O)O
- Mol. Weight (g/mol)
- 104.06
- CAS
- 141-82-2
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
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Datasets
- Osmotic coefficient (2)
- Mole fraction (2)
- ρl - Mass density, kg/m3 (4)
- γ - Surface tension liquid-gas, N/m (4)
- Binary diffusion coefficient, m2/s (2)
Osmotic coefficient [ref]
Operational conditions:
- Pressure, kPa = 20 (Liquid)
- Temperature, K = 298.1 (Liquid)
| Molality, mol/kg of Propanedioic acid (1) - Liquid | Osmotic coefficient - Liquid |
|---|---|
| 0.1216 | 1.1437 |
| 0.3009 | 0.4556 |
| 0.5079 | 0.2684 |
| 0.6604 | 0.2741 |
| 0.7994 | 0.3139 |
| 1.0104 | 0.3539 |
| 1.0796 | 0.3625 |
| 1.6311 | 0.3733 |
| 2.392 | 0.4014 |
| 3.1273 | 0.4365 |
| 4.097 | 0.4553 |
| 5.1201 | 0.4685 |
| 6.3693 | 0.4980 |
| 9.5447 | 0.5247 |
Osmotic coefficient [ref]
Operational conditions:
- Pressure, kPa = 20 (Liquid)
- Temperature, K = 298.1 (Liquid)
| Molality, mol/kg of Propanedioic acid (1) - Liquid | Osmotic coefficient - Liquid |
|---|---|
| 0.1216 | 1.1437 |
| 0.3009 | 0.4556 |
| 0.5079 | 0.2684 |
| 0.6604 | 0.2741 |
| 0.7994 | 0.3139 |
| 1.0104 | 0.3539 |
| 1.0796 | 0.3625 |
| 1.6311 | 0.3733 |
| 2.392 | 0.4014 |
| 3.1273 | 0.4365 |
| 4.097 | 0.4553 |
| 5.1201 | 0.4685 |
| 6.3693 | 0.4980 |
| 9.5447 | 0.5247 |
Mole fraction of Propanedioic acid (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid | Mole fraction of Propanedioic acid (1) - Liquid |
|---|---|
| 303.15 | 0.1263 |
| 308.15 | 0.1446 |
| 313.15 | 0.1628 |
| 318.15 | 0.1836 |
| 323.15 | 0.2081 |
| 328.15 | 0.2261 |
| 333.15 | 0.2442 |
Mole fraction of Propanedioic acid (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid | Mole fraction of Propanedioic acid (1) - Liquid |
|---|---|
| 303.15 | 0.1263 |
| 308.15 | 0.1446 |
| 313.15 | 0.1628 |
| 318.15 | 0.1836 |
| 323.15 | 0.2081 |
| 328.15 | 0.2261 |
| 333.15 | 0.2442 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Molality, mol/kg of Propanedioic acid (1) - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 0.0000 | 999.99 |
| 278.15 | 0.0100 | 1000.48 |
| 278.15 | 0.0200 | 1000.91 |
| 278.15 | 0.0300 | 1001.31 |
| 278.15 | 0.0396 | 1001.73 |
| 278.15 | 0.0500 | 1002.16 |
| 278.15 | 0.0594 | 1002.53 |
| 278.15 | 0.0693 | 1002.93 |
| 278.15 | 0.0795 | 1003.34 |
| 278.15 | 0.0891 | 1003.73 |
| 278.15 | 0.0993 | 1004.11 |
| 278.15 | 0.1984 | 1008.06 |
| 278.15 | 0.2977 | 1011.96 |
| 278.15 | 0.4040 | 1016.0 |
| 278.15 | 0.5055 | 1019.85 |
| 278.15 | 0.6055 | 1023.51 |
| 278.15 | 0.6936 | 1026.73 |
| 278.15 | 0.7926 | 1030.29 |
| 278.15 | 0.8910 | 1033.82 |
| 278.15 | 0.9895 | 1037.16 |
| 283.15 | 0.0000 | 999.73 |
| 283.15 | 0.0100 | 1000.21 |
| 283.15 | 0.0200 | 1000.62 |
| 283.15 | 0.0300 | 1001.0 |
| 283.15 | 0.0396 | 1001.4 |
| 283.15 | 0.0500 | 1001.83 |
| 283.15 | 0.0594 | 1002.19 |
| 283.15 | 0.0693 | 1002.58 |
| 283.15 | 0.0795 | 1002.98 |
| 283.15 | 0.0891 | 1003.36 |
| 283.15 | 0.0993 | 1003.73 |
| 283.15 | 0.1984 | 1007.6 |
| 283.15 | 0.2977 | 1011.4 |
| 283.15 | 0.4040 | 1015.36 |
| 283.15 | 0.5055 | 1019.12 |
| 283.15 | 0.6055 | 1022.71 |
| 283.15 | 0.6936 | 1025.86 |
| 283.15 | 0.7926 | 1029.35 |
| 283.15 | 0.8910 | 1032.8 |
| 283.15 | 0.9895 | 1036.1 |
| 288.15 | 0.0000 | 999.13 |
| 288.15 | 0.0100 | 999.61 |
| 288.15 | 0.0200 | 1000.03 |
| 288.15 | 0.0300 | 1000.4 |
| 288.15 | 0.0396 | 1000.79 |
| 288.15 | 0.0500 | 1001.21 |
| 288.15 | 0.0594 | 1001.57 |
| 288.15 | 0.0693 | 1001.95 |
| 288.15 | 0.0795 | 1002.34 |
| 288.15 | 0.0891 | 1002.71 |
| 288.15 | 0.0993 | 1003.07 |
| 288.15 | 0.1984 | 1006.87 |
| 288.15 | 0.2977 | 1010.6 |
| 288.15 | 0.4040 | 1014.47 |
| 288.15 | 0.5055 | 1018.15 |
| 288.15 | 0.6055 | 1021.67 |
| 288.15 | 0.6936 | 1024.77 |
| 288.15 | 0.7926 | 1028.19 |
| 288.15 | 0.8910 | 1031.58 |
| 288.15 | 0.9895 | 1034.82 |
| 293.15 | 0.0000 | 998.23 |
| 293.15 | 0.0100 | 998.7 |
| 293.15 | 0.0200 | 999.1 |
| 293.15 | 0.0300 | 999.47 |
| 293.15 | 0.0396 | 999.85 |
| 293.15 | 0.0500 | 1000.27 |
| 293.15 | 0.0594 | 1000.61 |
| 293.15 | 0.0693 | 1000.99 |
| 293.15 | 0.0795 | 1001.37 |
| 293.15 | 0.0891 | 1001.73 |
| 293.15 | 0.0993 | 1002.12 |
| 293.15 | 0.1984 | 1005.8 |
| 293.15 | 0.2977 | 1009.46 |
| 293.15 | 0.4040 | 1013.26 |
| 293.15 | 0.5055 | 1016.89 |
| 293.15 | 0.6055 | 1020.35 |
| 293.15 | 0.6936 | 1023.39 |
| 293.15 | 0.7926 | 1026.76 |
| 293.15 | 0.8910 | 1030.1 |
| 293.15 | 0.9895 | 1033.27 |
| 298.15 | 0.0000 | 997.05 |
| 298.15 | 0.0100 | 997.52 |
| 298.15 | 0.0200 | 997.93 |
| 298.15 | 0.0300 | 998.3 |
| 298.15 | 0.0396 | 998.66 |
| 298.15 | 0.0500 | 999.07 |
| 298.15 | 0.0594 | 999.4 |
| 298.15 | 0.0693 | 999.78 |
| 298.15 | 0.0795 | 1000.15 |
| 298.15 | 0.0891 | 1000.52 |
| 298.15 | 0.0993 | 1000.89 |
| 298.15 | 0.1984 | 1004.55 |
| 298.15 | 0.2977 | 1008.15 |
| 298.15 | 0.4040 | 1011.88 |
| 298.15 | 0.5055 | 1015.45 |
| 298.15 | 0.6055 | 1018.85 |
| 298.15 | 0.6936 | 1021.85 |
| 298.15 | 0.7926 | 1025.16 |
| 298.15 | 0.8910 | 1028.44 |
| 298.15 | 0.9895 | 1031.58 |
| 303.15 | 0.0000 | 995.68 |
| 303.15 | 0.0100 | 996.14 |
| 303.15 | 0.0200 | 996.53 |
| 303.15 | 0.0300 | 996.9 |
| 303.15 | 0.0396 | 997.28 |
| 303.15 | 0.0500 | 997.66 |
| 303.15 | 0.0594 | 997.99 |
| 303.15 | 0.0693 | 998.37 |
| 303.15 | 0.0795 | 998.72 |
| 303.15 | 0.0891 | 999.08 |
| 303.15 | 0.0993 | 999.45 |
| 303.15 | 0.1984 | 1003.05 |
| 303.15 | 0.2977 | 1006.6 |
| 303.15 | 0.4040 | 1010.27 |
| 303.15 | 0.5055 | 1013.79 |
| 303.15 | 0.6055 | 1017.14 |
| 303.15 | 0.6936 | 1020.08 |
| 303.15 | 0.7926 | 1023.35 |
| 303.15 | 0.8910 | 1026.58 |
| 303.15 | 0.9895 | 1029.66 |
| 308.15 | 0.0000 | 994.06 |
| 308.15 | 0.0100 | 994.51 |
| 308.15 | 0.0200 | 994.89 |
| 308.15 | 0.0300 | 995.23 |
| 308.15 | 0.0396 | 995.6 |
| 308.15 | 0.0500 | 996.0 |
| 308.15 | 0.0594 | 996.33 |
| 308.15 | 0.0693 | 996.69 |
| 308.15 | 0.0795 | 997.06 |
| 308.15 | 0.0891 | 997.4 |
| 308.15 | 0.0993 | 997.74 |
| 308.15 | 0.1984 | 1001.28 |
| 308.15 | 0.2977 | 1004.77 |
| 308.15 | 0.4040 | 1008.39 |
| 308.15 | 0.5055 | 1011.84 |
| 308.15 | 0.6055 | 1015.15 |
| 308.15 | 0.6936 | 1018.07 |
| 308.15 | 0.7926 | 1021.29 |
| 308.15 | 0.8910 | 1024.47 |
| 308.15 | 0.9895 | 1027.51 |
| 313.15 | 0.0000 | 992.24 |
| 313.15 | 0.0100 | 992.67 |
| 313.15 | 0.0200 | 993.03 |
| 313.15 | 0.0300 | 993.37 |
| 313.15 | 0.0396 | 993.74 |
| 313.15 | 0.0500 | 994.12 |
| 313.15 | 0.0594 | 994.45 |
| 313.15 | 0.0693 | 994.8 |
| 313.15 | 0.0795 | 995.16 |
| 313.15 | 0.0891 | 995.51 |
| 313.15 | 0.0993 | 995.86 |
| 313.15 | 0.1984 | 999.32 |
| 313.15 | 0.2977 | 1002.76 |
| 313.15 | 0.4040 | 1006.4 |
| 313.15 | 0.5055 | 1009.9 |
| 313.15 | 0.6055 | 1013.17 |
| 313.15 | 0.6936 | 1016.02 |
| 313.15 | 0.7926 | 1019.25 |
| 313.15 | 0.8910 | 1022.41 |
| 313.15 | 0.9895 | 1025.39 |
| 318.15 | 0.0000 | 990.24 |
| 318.15 | 0.0100 | 990.67 |
| 318.15 | 0.0200 | 991.04 |
| 318.15 | 0.0300 | 991.39 |
| 318.15 | 0.0396 | 991.75 |
| 318.15 | 0.0500 | 992.09 |
| 318.15 | 0.0594 | 992.44 |
| 318.15 | 0.0693 | 992.8 |
| 318.15 | 0.0795 | 993.16 |
| 318.15 | 0.0891 | 993.49 |
| 318.15 | 0.0993 | 993.83 |
| 318.15 | 0.1984 | 997.27 |
| 318.15 | 0.2977 | 1000.66 |
| 318.15 | 0.4040 | 1004.17 |
| 318.15 | 0.5055 | 1007.57 |
| 318.15 | 0.6055 | 1010.78 |
| 318.15 | 0.6936 | 1013.61 |
| 318.15 | 0.7926 | 1016.73 |
| 318.15 | 0.8910 | 1019.67 |
| 318.15 | 0.9895 | 1022.8 |
| 323.15 | 0.0000 | 988.07 |
| 323.15 | 0.0100 | 988.48 |
| 323.15 | 0.0200 | 988.85 |
| 323.15 | 0.0300 | 989.19 |
| 323.15 | 0.0396 | 989.54 |
| 323.15 | 0.0500 | 989.92 |
| 323.15 | 0.0594 | 990.24 |
| 323.15 | 0.0693 | 990.58 |
| 323.15 | 0.0795 | 990.94 |
| 323.15 | 0.0891 | 991.26 |
| 323.15 | 0.0993 | 991.63 |
| 323.15 | 0.1984 | 995.0 |
| 323.15 | 0.2977 | 998.36 |
| 323.15 | 0.4040 | 1001.82 |
| 323.15 | 0.5055 | 1005.17 |
| 323.15 | 0.6055 | 1008.36 |
| 323.15 | 0.6936 | 1011.15 |
| 323.15 | 0.7926 | 1014.23 |
| 323.15 | 0.8910 | 1017.35 |
| 323.15 | 0.9895 | 1020.22 |
| 328.15 | 0.0000 | 985.73 |
| 328.15 | 0.0100 | 986.12 |
| 328.15 | 0.0200 | 986.5 |
| 328.15 | 0.0300 | 986.83 |
| 328.15 | 0.0396 | 987.17 |
| 328.15 | 0.0500 | 987.55 |
| 328.15 | 0.0594 | 987.86 |
| 328.15 | 0.0693 | 988.21 |
| 328.15 | 0.0795 | 988.56 |
| 328.15 | 0.0891 | 988.89 |
| 328.15 | 0.0993 | 989.26 |
| 328.15 | 0.1984 | 992.58 |
| 328.15 | 0.2977 | 995.89 |
| 328.15 | 0.4040 | 999.32 |
| 328.15 | 0.5055 | 1002.63 |
| 328.15 | 0.6055 | 1005.78 |
| 328.15 | 0.6936 | 1008.54 |
| 328.15 | 0.7926 | 1011.64 |
| 328.15 | 0.8910 | 1014.68 |
| 328.15 | 0.9895 | 1017.49 |
| 333.15 | 0.0000 | 983.24 |
| 333.15 | 0.0100 | 983.63 |
| 333.15 | 0.0200 | 984.01 |
| 333.15 | 0.0300 | 984.34 |
| 333.15 | 0.0396 | 984.68 |
| 333.15 | 0.0500 | 985.05 |
| 333.15 | 0.0594 | 985.36 |
| 333.15 | 0.0693 | 985.69 |
| 333.15 | 0.0795 | 986.05 |
| 333.15 | 0.0891 | 986.37 |
| 333.15 | 0.0993 | 986.72 |
| 333.15 | 0.1984 | 990.02 |
| 333.15 | 0.2977 | 993.31 |
| 333.15 | 0.4040 | 996.78 |
| 333.15 | 0.5055 | 999.91 |
| 333.15 | 0.6055 | 1003.1 |
| 333.15 | 0.6936 | 1005.81 |
| 333.15 | 0.7926 | 1008.99 |
| 333.15 | 0.8910 | 1011.89 |
| 333.15 | 0.9895 | 1014.63 |
| 338.15 | 0.0000 | 980.59 |
| 338.15 | 0.0100 | 980.99 |
| 338.15 | 0.0200 | 981.37 |
| 338.15 | 0.0300 | 981.69 |
| 338.15 | 0.0396 | 982.03 |
| 338.15 | 0.0500 | 982.41 |
| 338.15 | 0.0594 | 982.72 |
| 338.15 | 0.0693 | 983.0 |
| 338.15 | 0.0795 | 983.39 |
| 338.15 | 0.0891 | 983.68 |
| 338.15 | 0.0993 | 984.02 |
| 338.15 | 0.1984 | 987.31 |
| 338.15 | 0.2977 | 990.55 |
| 338.15 | 0.4040 | 993.95 |
| 338.15 | 0.5055 | 997.16 |
| 338.15 | 0.6055 | 1000.24 |
| 338.15 | 0.6936 | 1002.93 |
| 338.15 | 0.7926 | 1006.0 |
| 338.15 | 0.8910 | 1008.94 |
| 338.15 | 0.9895 | 1011.16 |
| 343.15 | 0.0000 | 977.81 |
| 343.15 | 0.0100 | 978.22 |
| 343.15 | 0.0200 | 978.59 |
| 343.15 | 0.0300 | 978.9 |
| 343.15 | 0.0396 | 979.24 |
| 343.15 | 0.0500 | 979.6 |
| 343.15 | 0.0594 | 979.92 |
| 343.15 | 0.0693 | 980.22 |
| 343.15 | 0.0795 | 980.58 |
| 343.15 | 0.0891 | 980.9 |
| 343.15 | 0.0993 | 981.18 |
| 343.15 | 0.1984 | 984.49 |
| 343.15 | 0.2977 | 987.71 |
| 343.15 | 0.4040 | 991.05 |
| 343.15 | 0.5055 | 994.29 |
| 343.15 | 0.6055 | 997.39 |
| 343.15 | 0.6936 | 1000.21 |
| 343.15 | 0.7926 | 1002.97 |
| 343.15 | 0.8910 | 1005.93 |
| 343.15 | 0.9895 | 1008.49 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Propanedioic acid (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0090 | 1016.0 |
| 0.0300 | 1054.0 |
| 0.0410 | 1068.0 |
| 0.0550 | 1090.0 |
| 0.0690 | 1108.0 |
| 0.0850 | 1129.0 |
| 0.1020 | 1152.0 |
| 0.1470 | 1196.0 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Molality, mol/kg of Propanedioic acid (1) - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 0.0000 | 999.99 |
| 278.15 | 0.0100 | 1000.48 |
| 278.15 | 0.0200 | 1000.91 |
| 278.15 | 0.0300 | 1001.31 |
| 278.15 | 0.0396 | 1001.73 |
| 278.15 | 0.0500 | 1002.16 |
| 278.15 | 0.0594 | 1002.53 |
| 278.15 | 0.0693 | 1002.93 |
| 278.15 | 0.0795 | 1003.34 |
| 278.15 | 0.0891 | 1003.73 |
| 278.15 | 0.0993 | 1004.11 |
| 278.15 | 0.1984 | 1008.06 |
| 278.15 | 0.2977 | 1011.96 |
| 278.15 | 0.4040 | 1016.0 |
| 278.15 | 0.5055 | 1019.85 |
| 278.15 | 0.6055 | 1023.51 |
| 278.15 | 0.6936 | 1026.73 |
| 278.15 | 0.7926 | 1030.29 |
| 278.15 | 0.8910 | 1033.82 |
| 278.15 | 0.9895 | 1037.16 |
| 283.15 | 0.0000 | 999.73 |
| 283.15 | 0.0100 | 1000.21 |
| 283.15 | 0.0200 | 1000.62 |
| 283.15 | 0.0300 | 1001.0 |
| 283.15 | 0.0396 | 1001.4 |
| 283.15 | 0.0500 | 1001.83 |
| 283.15 | 0.0594 | 1002.19 |
| 283.15 | 0.0693 | 1002.58 |
| 283.15 | 0.0795 | 1002.98 |
| 283.15 | 0.0891 | 1003.36 |
| 283.15 | 0.0993 | 1003.73 |
| 283.15 | 0.1984 | 1007.6 |
| 283.15 | 0.2977 | 1011.4 |
| 283.15 | 0.4040 | 1015.36 |
| 283.15 | 0.5055 | 1019.12 |
| 283.15 | 0.6055 | 1022.71 |
| 283.15 | 0.6936 | 1025.86 |
| 283.15 | 0.7926 | 1029.35 |
| 283.15 | 0.8910 | 1032.8 |
| 283.15 | 0.9895 | 1036.1 |
| 288.15 | 0.0000 | 999.13 |
| 288.15 | 0.0100 | 999.61 |
| 288.15 | 0.0200 | 1000.03 |
| 288.15 | 0.0300 | 1000.4 |
| 288.15 | 0.0396 | 1000.79 |
| 288.15 | 0.0500 | 1001.21 |
| 288.15 | 0.0594 | 1001.57 |
| 288.15 | 0.0693 | 1001.95 |
| 288.15 | 0.0795 | 1002.34 |
| 288.15 | 0.0891 | 1002.71 |
| 288.15 | 0.0993 | 1003.07 |
| 288.15 | 0.1984 | 1006.87 |
| 288.15 | 0.2977 | 1010.6 |
| 288.15 | 0.4040 | 1014.47 |
| 288.15 | 0.5055 | 1018.15 |
| 288.15 | 0.6055 | 1021.67 |
| 288.15 | 0.6936 | 1024.77 |
| 288.15 | 0.7926 | 1028.19 |
| 288.15 | 0.8910 | 1031.58 |
| 288.15 | 0.9895 | 1034.82 |
| 293.15 | 0.0000 | 998.23 |
| 293.15 | 0.0100 | 998.7 |
| 293.15 | 0.0200 | 999.1 |
| 293.15 | 0.0300 | 999.47 |
| 293.15 | 0.0396 | 999.85 |
| 293.15 | 0.0500 | 1000.27 |
| 293.15 | 0.0594 | 1000.61 |
| 293.15 | 0.0693 | 1000.99 |
| 293.15 | 0.0795 | 1001.37 |
| 293.15 | 0.0891 | 1001.73 |
| 293.15 | 0.0993 | 1002.12 |
| 293.15 | 0.1984 | 1005.8 |
| 293.15 | 0.2977 | 1009.46 |
| 293.15 | 0.4040 | 1013.26 |
| 293.15 | 0.5055 | 1016.89 |
| 293.15 | 0.6055 | 1020.35 |
| 293.15 | 0.6936 | 1023.39 |
| 293.15 | 0.7926 | 1026.76 |
| 293.15 | 0.8910 | 1030.1 |
| 293.15 | 0.9895 | 1033.27 |
| 298.15 | 0.0000 | 997.05 |
| 298.15 | 0.0100 | 997.52 |
| 298.15 | 0.0200 | 997.93 |
| 298.15 | 0.0300 | 998.3 |
| 298.15 | 0.0396 | 998.66 |
| 298.15 | 0.0500 | 999.07 |
| 298.15 | 0.0594 | 999.4 |
| 298.15 | 0.0693 | 999.78 |
| 298.15 | 0.0795 | 1000.15 |
| 298.15 | 0.0891 | 1000.52 |
| 298.15 | 0.0993 | 1000.89 |
| 298.15 | 0.1984 | 1004.55 |
| 298.15 | 0.2977 | 1008.15 |
| 298.15 | 0.4040 | 1011.88 |
| 298.15 | 0.5055 | 1015.45 |
| 298.15 | 0.6055 | 1018.85 |
| 298.15 | 0.6936 | 1021.85 |
| 298.15 | 0.7926 | 1025.16 |
| 298.15 | 0.8910 | 1028.44 |
| 298.15 | 0.9895 | 1031.58 |
| 303.15 | 0.0000 | 995.68 |
| 303.15 | 0.0100 | 996.14 |
| 303.15 | 0.0200 | 996.53 |
| 303.15 | 0.0300 | 996.9 |
| 303.15 | 0.0396 | 997.28 |
| 303.15 | 0.0500 | 997.66 |
| 303.15 | 0.0594 | 997.99 |
| 303.15 | 0.0693 | 998.37 |
| 303.15 | 0.0795 | 998.72 |
| 303.15 | 0.0891 | 999.08 |
| 303.15 | 0.0993 | 999.45 |
| 303.15 | 0.1984 | 1003.05 |
| 303.15 | 0.2977 | 1006.6 |
| 303.15 | 0.4040 | 1010.27 |
| 303.15 | 0.5055 | 1013.79 |
| 303.15 | 0.6055 | 1017.14 |
| 303.15 | 0.6936 | 1020.08 |
| 303.15 | 0.7926 | 1023.35 |
| 303.15 | 0.8910 | 1026.58 |
| 303.15 | 0.9895 | 1029.66 |
| 308.15 | 0.0000 | 994.06 |
| 308.15 | 0.0100 | 994.51 |
| 308.15 | 0.0200 | 994.89 |
| 308.15 | 0.0300 | 995.23 |
| 308.15 | 0.0396 | 995.6 |
| 308.15 | 0.0500 | 996.0 |
| 308.15 | 0.0594 | 996.33 |
| 308.15 | 0.0693 | 996.69 |
| 308.15 | 0.0795 | 997.06 |
| 308.15 | 0.0891 | 997.4 |
| 308.15 | 0.0993 | 997.74 |
| 308.15 | 0.1984 | 1001.28 |
| 308.15 | 0.2977 | 1004.77 |
| 308.15 | 0.4040 | 1008.39 |
| 308.15 | 0.5055 | 1011.84 |
| 308.15 | 0.6055 | 1015.15 |
| 308.15 | 0.6936 | 1018.07 |
| 308.15 | 0.7926 | 1021.29 |
| 308.15 | 0.8910 | 1024.47 |
| 308.15 | 0.9895 | 1027.51 |
| 313.15 | 0.0000 | 992.24 |
| 313.15 | 0.0100 | 992.67 |
| 313.15 | 0.0200 | 993.03 |
| 313.15 | 0.0300 | 993.37 |
| 313.15 | 0.0396 | 993.74 |
| 313.15 | 0.0500 | 994.12 |
| 313.15 | 0.0594 | 994.45 |
| 313.15 | 0.0693 | 994.8 |
| 313.15 | 0.0795 | 995.16 |
| 313.15 | 0.0891 | 995.51 |
| 313.15 | 0.0993 | 995.86 |
| 313.15 | 0.1984 | 999.32 |
| 313.15 | 0.2977 | 1002.76 |
| 313.15 | 0.4040 | 1006.4 |
| 313.15 | 0.5055 | 1009.9 |
| 313.15 | 0.6055 | 1013.17 |
| 313.15 | 0.6936 | 1016.02 |
| 313.15 | 0.7926 | 1019.25 |
| 313.15 | 0.8910 | 1022.41 |
| 313.15 | 0.9895 | 1025.39 |
| 318.15 | 0.0000 | 990.24 |
| 318.15 | 0.0100 | 990.67 |
| 318.15 | 0.0200 | 991.04 |
| 318.15 | 0.0300 | 991.39 |
| 318.15 | 0.0396 | 991.75 |
| 318.15 | 0.0500 | 992.09 |
| 318.15 | 0.0594 | 992.44 |
| 318.15 | 0.0693 | 992.8 |
| 318.15 | 0.0795 | 993.16 |
| 318.15 | 0.0891 | 993.49 |
| 318.15 | 0.0993 | 993.83 |
| 318.15 | 0.1984 | 997.27 |
| 318.15 | 0.2977 | 1000.66 |
| 318.15 | 0.4040 | 1004.17 |
| 318.15 | 0.5055 | 1007.57 |
| 318.15 | 0.6055 | 1010.78 |
| 318.15 | 0.6936 | 1013.61 |
| 318.15 | 0.7926 | 1016.73 |
| 318.15 | 0.8910 | 1019.67 |
| 318.15 | 0.9895 | 1022.8 |
| 323.15 | 0.0000 | 988.07 |
| 323.15 | 0.0100 | 988.48 |
| 323.15 | 0.0200 | 988.85 |
| 323.15 | 0.0300 | 989.19 |
| 323.15 | 0.0396 | 989.54 |
| 323.15 | 0.0500 | 989.92 |
| 323.15 | 0.0594 | 990.24 |
| 323.15 | 0.0693 | 990.58 |
| 323.15 | 0.0795 | 990.94 |
| 323.15 | 0.0891 | 991.26 |
| 323.15 | 0.0993 | 991.63 |
| 323.15 | 0.1984 | 995.0 |
| 323.15 | 0.2977 | 998.36 |
| 323.15 | 0.4040 | 1001.82 |
| 323.15 | 0.5055 | 1005.17 |
| 323.15 | 0.6055 | 1008.36 |
| 323.15 | 0.6936 | 1011.15 |
| 323.15 | 0.7926 | 1014.23 |
| 323.15 | 0.8910 | 1017.35 |
| 323.15 | 0.9895 | 1020.22 |
| 328.15 | 0.0000 | 985.73 |
| 328.15 | 0.0100 | 986.12 |
| 328.15 | 0.0200 | 986.5 |
| 328.15 | 0.0300 | 986.83 |
| 328.15 | 0.0396 | 987.17 |
| 328.15 | 0.0500 | 987.55 |
| 328.15 | 0.0594 | 987.86 |
| 328.15 | 0.0693 | 988.21 |
| 328.15 | 0.0795 | 988.56 |
| 328.15 | 0.0891 | 988.89 |
| 328.15 | 0.0993 | 989.26 |
| 328.15 | 0.1984 | 992.58 |
| 328.15 | 0.2977 | 995.89 |
| 328.15 | 0.4040 | 999.32 |
| 328.15 | 0.5055 | 1002.63 |
| 328.15 | 0.6055 | 1005.78 |
| 328.15 | 0.6936 | 1008.54 |
| 328.15 | 0.7926 | 1011.64 |
| 328.15 | 0.8910 | 1014.68 |
| 328.15 | 0.9895 | 1017.49 |
| 333.15 | 0.0000 | 983.24 |
| 333.15 | 0.0100 | 983.63 |
| 333.15 | 0.0200 | 984.01 |
| 333.15 | 0.0300 | 984.34 |
| 333.15 | 0.0396 | 984.68 |
| 333.15 | 0.0500 | 985.05 |
| 333.15 | 0.0594 | 985.36 |
| 333.15 | 0.0693 | 985.69 |
| 333.15 | 0.0795 | 986.05 |
| 333.15 | 0.0891 | 986.37 |
| 333.15 | 0.0993 | 986.72 |
| 333.15 | 0.1984 | 990.02 |
| 333.15 | 0.2977 | 993.31 |
| 333.15 | 0.4040 | 996.78 |
| 333.15 | 0.5055 | 999.91 |
| 333.15 | 0.6055 | 1003.1 |
| 333.15 | 0.6936 | 1005.81 |
| 333.15 | 0.7926 | 1008.99 |
| 333.15 | 0.8910 | 1011.89 |
| 333.15 | 0.9895 | 1014.63 |
| 338.15 | 0.0000 | 980.59 |
| 338.15 | 0.0100 | 980.99 |
| 338.15 | 0.0200 | 981.37 |
| 338.15 | 0.0300 | 981.69 |
| 338.15 | 0.0396 | 982.03 |
| 338.15 | 0.0500 | 982.41 |
| 338.15 | 0.0594 | 982.72 |
| 338.15 | 0.0693 | 983.0 |
| 338.15 | 0.0795 | 983.39 |
| 338.15 | 0.0891 | 983.68 |
| 338.15 | 0.0993 | 984.02 |
| 338.15 | 0.1984 | 987.31 |
| 338.15 | 0.2977 | 990.55 |
| 338.15 | 0.4040 | 993.95 |
| 338.15 | 0.5055 | 997.16 |
| 338.15 | 0.6055 | 1000.24 |
| 338.15 | 0.6936 | 1002.93 |
| 338.15 | 0.7926 | 1006.0 |
| 338.15 | 0.8910 | 1008.94 |
| 338.15 | 0.9895 | 1011.16 |
| 343.15 | 0.0000 | 977.81 |
| 343.15 | 0.0100 | 978.22 |
| 343.15 | 0.0200 | 978.59 |
| 343.15 | 0.0300 | 978.9 |
| 343.15 | 0.0396 | 979.24 |
| 343.15 | 0.0500 | 979.6 |
| 343.15 | 0.0594 | 979.92 |
| 343.15 | 0.0693 | 980.22 |
| 343.15 | 0.0795 | 980.58 |
| 343.15 | 0.0891 | 980.9 |
| 343.15 | 0.0993 | 981.18 |
| 343.15 | 0.1984 | 984.49 |
| 343.15 | 0.2977 | 987.71 |
| 343.15 | 0.4040 | 991.05 |
| 343.15 | 0.5055 | 994.29 |
| 343.15 | 0.6055 | 997.39 |
| 343.15 | 0.6936 | 1000.21 |
| 343.15 | 0.7926 | 1002.97 |
| 343.15 | 0.8910 | 1005.93 |
| 343.15 | 0.9895 | 1008.49 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Propanedioic acid (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0090 | 1016.0 |
| 0.0300 | 1054.0 |
| 0.0410 | 1068.0 |
| 0.0550 | 1090.0 |
| 0.0690 | 1108.0 |
| 0.0850 | 1129.0 |
| 0.1020 | 1152.0 |
| 0.1470 | 1196.0 |
Surface tension liquid-gas, N/m [ref]
Operational condition: Temperature, K = 298 (Liquid)
| Mole fraction of Propanedioic acid (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0100 | 0.0692 |
| 0.0170 | 0.0685 |
| 0.0250 | 0.0667 |
| 0.0330 | 0.0667 |
| 0.0400 | 0.0656 |
| 0.0500 | 0.0656 |
| 0.0550 | 0.0655 |
| 0.0650 | 0.0650 |
| 0.0700 | 0.0642 |
| 0.0800 | 0.0635 |
| 0.0880 | 0.0642 |
| 0.0940 | 0.0635 |
| 0.1070 | 0.0627 |
| 0.1220 | 0.0623 |
| 0.1370 | 0.0622 |
| 0.1490 | 0.0626 |
| 0.1580 | 0.0622 |
Surface tension liquid-gas, N/m [ref]
Operational condition: Mole fraction = 0.06 (Liquid)
| Temperature, K - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 278.10 | 0.0665 |
| 279.30 | 0.0660 |
| 279.70 | 0.0659 |
| 282.60 | 0.0660 |
| 285.00 | 0.0657 |
| 286.50 | 0.0656 |
| 287.80 | 0.0654 |
| 288.70 | 0.0652 |
| 289.60 | 0.0653 |
| 290.90 | 0.0646 |
| 291.10 | 0.0650 |
| 293.00 | 0.0646 |
| 295.30 | 0.0647 |
| 296.70 | 0.0641 |
| 297.10 | 0.0641 |
| 298.20 | 0.0638 |
| 299.00 | 0.0636 |
| 299.10 | 0.0639 |
| 301.20 | 0.0640 |
| 303.30 | 0.0630 |
Surface tension liquid-gas, N/m [ref]
Operational condition: Temperature, K = 298 (Liquid)
| Mole fraction of Propanedioic acid (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0100 | 0.0692 |
| 0.0170 | 0.0685 |
| 0.0250 | 0.0667 |
| 0.0330 | 0.0667 |
| 0.0400 | 0.0656 |
| 0.0500 | 0.0656 |
| 0.0550 | 0.0655 |
| 0.0650 | 0.0650 |
| 0.0700 | 0.0642 |
| 0.0800 | 0.0635 |
| 0.0880 | 0.0642 |
| 0.0940 | 0.0635 |
| 0.1070 | 0.0627 |
| 0.1220 | 0.0623 |
| 0.1370 | 0.0622 |
| 0.1490 | 0.0626 |
| 0.1580 | 0.0622 |
Surface tension liquid-gas, N/m [ref]
Operational condition: Mole fraction = 0.06 (Liquid)
| Temperature, K - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 278.10 | 0.0665 |
| 279.30 | 0.0660 |
| 279.70 | 0.0659 |
| 282.60 | 0.0660 |
| 285.00 | 0.0657 |
| 286.50 | 0.0656 |
| 287.80 | 0.0654 |
| 288.70 | 0.0652 |
| 289.60 | 0.0653 |
| 290.90 | 0.0646 |
| 291.10 | 0.0650 |
| 293.00 | 0.0646 |
| 295.30 | 0.0647 |
| 296.70 | 0.0641 |
| 297.10 | 0.0641 |
| 298.20 | 0.0638 |
| 299.00 | 0.0636 |
| 299.10 | 0.0639 |
| 301.20 | 0.0640 |
| 303.30 | 0.0630 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Amount concentration (molarity), mol/dm3 of Propanedioic acid (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0001 | 0.0000 |
| 0.0001 | 0.0000 |
| 0.0001 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0004 | 0.0000 |
| 0.0004 | 0.0000 |
| 0.0004 | 0.0000 |
| 0.0005 | 0.0000 |
| 0.0005 | 0.0000 |
| 0.0005 | 0.0000 |
| 0.0006 | 0.0000 |
| 0.0006 | 0.0000 |
| 0.0008 | 0.0000 |
| 0.0008 | 0.0000 |
| 0.0008 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0019 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0045 | 0.0000 |
| 0.0046 | 0.0000 |
| 0.0046 | 0.0000 |
| 0.0046 | 0.0000 |
| 0.0070 | 0.0000 |
| 0.0070 | 0.0000 |
| 0.0101 | 0.0000 |
| 0.0118 | 0.0000 |
| 0.0118 | 0.0000 |
| 0.0118 | 0.0000 |
| 0.0150 | 0.0000 |
| 0.0150 | 0.0000 |
| 0.0150 | 0.0000 |
| 0.0201 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Amount concentration (molarity), mol/dm3 of Propanedioic acid (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0001 | 0.0000 |
| 0.0001 | 0.0000 |
| 0.0001 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0003 | 0.0000 |
| 0.0004 | 0.0000 |
| 0.0004 | 0.0000 |
| 0.0004 | 0.0000 |
| 0.0005 | 0.0000 |
| 0.0005 | 0.0000 |
| 0.0005 | 0.0000 |
| 0.0006 | 0.0000 |
| 0.0006 | 0.0000 |
| 0.0008 | 0.0000 |
| 0.0008 | 0.0000 |
| 0.0008 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0014 | 0.0000 |
| 0.0019 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0025 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0035 | 0.0000 |
| 0.0045 | 0.0000 |
| 0.0046 | 0.0000 |
| 0.0046 | 0.0000 |
| 0.0046 | 0.0000 |
| 0.0070 | 0.0000 |
| 0.0070 | 0.0000 |
| 0.0101 | 0.0000 |
| 0.0118 | 0.0000 |
| 0.0118 | 0.0000 |
| 0.0118 | 0.0000 |
| 0.0150 | 0.0000 |
| 0.0150 | 0.0000 |
| 0.0150 | 0.0000 |
| 0.0201 | 0.0000 |
Sources
- Solubility of citric, malonic, and malic acids in different solvents from 303.2 to 333.2 K
- Experiment and correlation of osmotic coefficient for aqueous solution of carboxylic acids using NRTL nonrandom factor model
- Volumetric properties of aqueous solutions of malonic acid
- Surface Tensions and Densities of Oxalic, Malonic, Succinic, Maleic, Malic, and cis-Pinonic Acids
- Mutual Diffusion Coefficients for Binary Aqueous Solutions of Arsenous, Arsenic, and Malonic Acids