Datasets
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Molality, mol/kg (6)
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σcond - Electrical conductivity, S/m (2)
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Molar enthalpy (2)
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Binary diffusion coefficient, m2/s (2)
Molality, mol/kg
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Temperature, K - Liquid |
Molality, mol/kg - Liquid |
| 293.15 |
0.1182 |
| 298.15 |
0.1215 |
| 303.15 |
0.1273 |
| 308.15 |
0.1327 |
| 313.15 |
0.1360 |
| 318.15 |
0.1424 |
Mole fraction of Benzoic acid, 3,4-dihydroxy- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Temperature, K - Liquid |
Mole fraction of Benzoic acid, 3,4-dihydroxy- (1) - Liquid |
| 293.15 |
0.0021 |
| 298.15 |
0.0022 |
| 303.15 |
0.0023 |
| 308.15 |
0.0024 |
| 313.15 |
0.0024 |
| 318.15 |
0.0026 |
Mass concentration, kg/m3
[ref]
| Temperature, K - Liquid |
Mass concentration, kg/m3 - Liquid |
| 298.75 |
29.4 |
| 314.65 |
44.3 |
| 334.95 |
95.3 |
| 355.25 |
175.0 |
| 375.35 |
305.0 |
| 395.65 |
773.0 |
| 415.85 |
1180.0 |
Molality, mol/kg
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Temperature, K - Liquid |
Molality, mol/kg - Liquid |
| 293.15 |
0.1182 |
| 298.15 |
0.1215 |
| 303.15 |
0.1273 |
| 308.15 |
0.1327 |
| 313.15 |
0.1360 |
| 318.15 |
0.1424 |
Mole fraction of Benzoic acid, 3,4-dihydroxy- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Temperature, K - Liquid |
Mole fraction of Benzoic acid, 3,4-dihydroxy- (1) - Liquid |
| 293.15 |
0.0021 |
| 298.15 |
0.0022 |
| 303.15 |
0.0023 |
| 308.15 |
0.0024 |
| 313.15 |
0.0024 |
| 318.15 |
0.0026 |
Mass concentration, kg/m3
[ref]
| Temperature, K - Liquid |
Mass concentration, kg/m3 - Liquid |
| 298.75 |
29.4 |
| 314.65 |
44.3 |
| 334.95 |
95.3 |
| 355.25 |
175.0 |
| 375.35 |
305.0 |
| 395.65 |
773.0 |
| 415.85 |
1180.0 |
Electrical conductivity, S/m
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Benzoic acid, 3,4-dihydroxy- (1) - Liquid |
Electrical conductivity, S/m - Liquid |
| 288.15 |
0.0010 |
0.0048 |
| 288.15 |
0.0020 |
0.0070 |
| 288.15 |
0.0040 |
0.0102 |
| 288.15 |
0.0060 |
0.0126 |
| 288.15 |
0.0080 |
0.0146 |
| 288.15 |
0.0100 |
0.0164 |
| 291.15 |
0.0010 |
0.0051 |
| 291.15 |
0.0020 |
0.0074 |
| 291.15 |
0.0040 |
0.0107 |
| 291.15 |
0.0060 |
0.0132 |
| 291.15 |
0.0080 |
0.0154 |
| 291.15 |
0.0100 |
0.0173 |
| 294.15 |
0.0010 |
0.0054 |
| 294.15 |
0.0020 |
0.0078 |
| 294.15 |
0.0040 |
0.0113 |
| 294.15 |
0.0060 |
0.0140 |
| 294.15 |
0.0080 |
0.0162 |
| 294.15 |
0.0100 |
0.0182 |
| 298.15 |
0.0010 |
0.0058 |
| 298.15 |
0.0020 |
0.0084 |
| 298.15 |
0.0040 |
0.0121 |
| 298.15 |
0.0060 |
0.0150 |
| 298.15 |
0.0080 |
0.0174 |
| 298.15 |
0.0100 |
0.0196 |
Electrical conductivity, S/m
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Benzoic acid, 3,4-dihydroxy- (1) - Liquid |
Electrical conductivity, S/m - Liquid |
| 288.15 |
0.0010 |
0.0048 |
| 288.15 |
0.0020 |
0.0070 |
| 288.15 |
0.0040 |
0.0102 |
| 288.15 |
0.0060 |
0.0126 |
| 288.15 |
0.0080 |
0.0146 |
| 288.15 |
0.0100 |
0.0164 |
| 291.15 |
0.0010 |
0.0051 |
| 291.15 |
0.0020 |
0.0074 |
| 291.15 |
0.0040 |
0.0107 |
| 291.15 |
0.0060 |
0.0132 |
| 291.15 |
0.0080 |
0.0154 |
| 291.15 |
0.0100 |
0.0173 |
| 294.15 |
0.0010 |
0.0054 |
| 294.15 |
0.0020 |
0.0078 |
| 294.15 |
0.0040 |
0.0113 |
| 294.15 |
0.0060 |
0.0140 |
| 294.15 |
0.0080 |
0.0162 |
| 294.15 |
0.0100 |
0.0182 |
| 298.15 |
0.0010 |
0.0058 |
| 298.15 |
0.0020 |
0.0084 |
| 298.15 |
0.0040 |
0.0121 |
| 298.15 |
0.0060 |
0.0150 |
| 298.15 |
0.0080 |
0.0174 |
| 298.15 |
0.0100 |
0.0196 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Fixed |
Measured |
| Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.0250 |
0.0118 |
0.2930 |
| 0.0300 |
0.0142 |
0.3325 |
| 0.0400 |
0.0189 |
0.4086 |
| 0.0450 |
0.0212 |
0.4462 |
| 0.0500 |
0.0236 |
0.4796 |
| 0.0550 |
0.0260 |
0.5123 |
| 0.0600 |
0.0282 |
0.5454 |
| 0.0650 |
0.0306 |
0.5752 |
| 0.0700 |
0.0330 |
0.6037 |
| 0.0750 |
0.0354 |
0.6297 |
| 0.0800 |
0.0377 |
0.6552 |
| 0.0900 |
0.0424 |
0.7003 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Fixed |
Measured |
| Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.0250 |
0.0118 |
0.2930 |
| 0.0300 |
0.0142 |
0.3325 |
| 0.0400 |
0.0189 |
0.4086 |
| 0.0450 |
0.0212 |
0.4462 |
| 0.0500 |
0.0236 |
0.4796 |
| 0.0550 |
0.0260 |
0.5123 |
| 0.0600 |
0.0282 |
0.5454 |
| 0.0650 |
0.0306 |
0.5752 |
| 0.0700 |
0.0330 |
0.6037 |
| 0.0750 |
0.0354 |
0.6297 |
| 0.0800 |
0.0377 |
0.6552 |
| 0.0900 |
0.0424 |
0.7003 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Mole fraction = 0 (Fluid (supercritical or subcritical phases))
- Pressure, kPa = 101 (Fluid (supercritical or subcritical phases))
| Temperature, K - Fluid (supercritical or subcritical phases) |
Binary diffusion coefficient, m2/s - Fluid (supercritical or subcritical phases) |
| 298.00 |
0.0000 |
| 312.00 |
0.0000 |
| 332.00 |
0.0000 |
| 352.00 |
0.0000 |
| 372.00 |
0.0000 |
| 392.00 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Mole fraction = 0 (Fluid (supercritical or subcritical phases))
- Pressure, kPa = 101 (Fluid (supercritical or subcritical phases))
| Temperature, K - Fluid (supercritical or subcritical phases) |
Binary diffusion coefficient, m2/s - Fluid (supercritical or subcritical phases) |
| 298.00 |
0.0000 |
| 312.00 |
0.0000 |
| 332.00 |
0.0000 |
| 352.00 |
0.0000 |
| 372.00 |
0.0000 |
| 392.00 |
0.0000 |
Sources