Datasets
-
Activity coefficient (4)
-
Mole fraction (40)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Interfacial tension, N/m (8)
-
ρl - Mass density, kg/m3 (4)
Activity coefficient of Toluene (1)
[ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Toluene (1) - Liquid |
| 288.15 |
8976.0 |
| 298.15 |
8954.0 |
| 308.15 |
8775.0 |
| 318.15 |
8290.0 |
Activity coefficient of Toluene (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Toluene (1) - Liquid |
| 308.95 |
8570.0 |
| 313.25 |
8090.0 |
| 318.25 |
7720.0 |
| 323.15 |
7110.0 |
Activity coefficient of Toluene (1)
[ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Toluene (1) - Liquid |
| 288.15 |
8976.0 |
| 298.15 |
8954.0 |
| 308.15 |
8775.0 |
| 318.15 |
8290.0 |
Activity coefficient of Toluene (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Toluene (1) - Liquid |
| 308.95 |
8570.0 |
| 313.25 |
8090.0 |
| 318.25 |
7720.0 |
| 323.15 |
7110.0 |
Mole fraction of Toluene (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 288.50 |
0.0001 |
| 292.60 |
0.0001 |
| 301.80 |
0.0002 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 297.60 |
7074.00 |
0.0001 |
| 297.60 |
10706.00 |
0.0001 |
| 297.62 |
3810.00 |
0.0001 |
| 297.64 |
513.30 |
0.0001 |
| 312.56 |
508.50 |
0.0001 |
| 312.59 |
1010.00 |
0.0001 |
| 343.18 |
521.50 |
0.0002 |
| 372.76 |
508.40 |
0.0003 |
| 392.81 |
7564.00 |
0.0004 |
| 392.82 |
10303.00 |
0.0004 |
| 392.84 |
520.90 |
0.0004 |
| 392.84 |
2570.00 |
0.0004 |
| 392.84 |
5129.00 |
0.0004 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 295.70 |
101.00 |
0.0001 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 101.30 |
303.15 |
0.0035 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 2 |
Temperature, K - Liquid mixture 2 |
Mole fraction of Toluene (1) - Liquid mixture 2 |
| 101.30 |
303.15 |
0.0001 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 2 |
| 273.15 |
1.50 |
0.0001 |
| 283.15 |
2.90 |
0.0001 |
| 298.15 |
7.00 |
0.0001 |
| 298.15 |
7.00 |
0.0001 |
| 305.35 |
10.20 |
0.0001 |
| 313.15 |
15.00 |
0.0001 |
| 333.15 |
38.00 |
0.0002 |
| 348.15 |
71.00 |
0.0002 |
| 373.15 |
175.00 |
0.0003 |
| 373.15 |
175.00 |
0.0003 |
| 398.15 |
383.00 |
0.0004 |
| 398.15 |
383.00 |
0.0004 |
| 413.15 |
580.00 |
0.0007 |
| 423.15 |
750.00 |
0.0008 |
| 453.15 |
1520.00 |
0.0015 |
| 458.15 |
1700.00 |
0.0017 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 273.15 |
1.50 |
0.0012 |
| 283.15 |
2.90 |
0.0017 |
| 298.15 |
7.00 |
0.0027 |
| 298.15 |
7.00 |
0.0027 |
| 305.35 |
10.20 |
0.0033 |
| 313.15 |
15.00 |
0.0043 |
| 333.15 |
38.00 |
0.0079 |
| 348.15 |
71.00 |
0.0122 |
| 373.15 |
175.00 |
0.0226 |
| 373.15 |
175.00 |
0.0239 |
| 398.15 |
383.00 |
0.0427 |
| 398.15 |
383.00 |
0.0425 |
| 413.15 |
580.00 |
0.0598 |
| 423.15 |
750.00 |
0.0692 |
| 453.15 |
1520.00 |
0.1202 |
| 458.15 |
1700.00 |
0.1328 |
Mole fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298 (Liquid mixture 1)
| Mole fraction of Water (2) - Liquid mixture 1 |
| 0.9923 |
| 0.1533 |
Mole fraction of Toluene (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298 (Liquid mixture 1)
| Mole fraction of Toluene (1) - Liquid mixture 1 |
| 0.0017 |
| 0.9570 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.15 |
0.0033 |
| 323.15 |
0.0067 |
| 373.25 |
0.0224 |
| 401.75 |
0.0410 |
| 423.45 |
0.0730 |
| 446.95 |
0.1070 |
Mole fraction of Toluene (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 298.15 |
0.0001 |
| 298.15 |
0.9970 |
| 333.15 |
0.0002 |
| 333.15 |
0.9930 |
Henry's Law constant (mole fraction scale), kPa of Toluene (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of Toluene (1) - Liquid |
| 322.00 |
85500.0 |
| 342.00 |
138800.0 |
| 362.00 |
214900.0 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0005 |
| 298.15 |
0.0009 |
| 313.15 |
0.0008 |
| 323.15 |
0.0006 |
| 323.15 |
0.0009 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 323.15 |
0.9990 |
| 313.15 |
0.9992 |
Henry's Law constant (molality scale), kPa*kg/mol of Toluene (1)
[ref]
Operational condition: Molality, mol/kg =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Toluene (1) - Liquid |
| 274.15 |
164.26 |
| 294.65 |
458.78 |
| 294.65 |
470.21 |
| 296.15 |
489.35 |
| 310.15 |
315.95 |
| 313.15 |
981.98 |
| 326.15 |
1835.68 |
| 331.15 |
3025.01 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 303.20 |
0.0013 |
| 313.20 |
0.0014 |
| 323.20 |
0.0022 |
| 333.20 |
0.0025 |
| 343.20 |
0.0050 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 303.20 |
0.9969 |
| 313.20 |
0.9958 |
| 323.20 |
0.9942 |
| 333.20 |
0.9935 |
| 343.20 |
0.9914 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 293.70 |
0.0023 |
| 303.30 |
0.0030 |
| 308.20 |
0.0032 |
| 313.50 |
0.0038 |
| 317.60 |
0.0044 |
| 324.20 |
0.0049 |
| 327.60 |
0.0055 |
| 334.10 |
0.0067 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 297.80 |
115.00 |
0.0001 |
| 324.00 |
199.00 |
0.0001 |
| 350.60 |
197.00 |
0.0002 |
| 376.10 |
167.00 |
0.0003 |
| 401.60 |
792.00 |
0.0004 |
| 431.90 |
1261.00 |
0.0007 |
| 461.00 |
2040.00 |
0.0014 |
| 490.40 |
3800.00 |
0.0025 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.50 |
112.00 |
0.0030 |
| 324.30 |
201.00 |
0.0055 |
| 350.90 |
358.00 |
0.0115 |
| 376.60 |
478.00 |
0.0222 |
| 401.50 |
716.00 |
0.0411 |
| 431.70 |
1450.00 |
0.0779 |
| 461.80 |
3076.00 |
0.1540 |
| 491.40 |
4733.00 |
0.2520 |
Mole fraction of Toluene (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 288.50 |
0.0001 |
| 292.60 |
0.0001 |
| 301.80 |
0.0002 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 297.60 |
7074.00 |
0.0001 |
| 297.60 |
10706.00 |
0.0001 |
| 297.62 |
3810.00 |
0.0001 |
| 297.64 |
513.30 |
0.0001 |
| 312.56 |
508.50 |
0.0001 |
| 312.59 |
1010.00 |
0.0001 |
| 343.18 |
521.50 |
0.0002 |
| 372.76 |
508.40 |
0.0003 |
| 392.81 |
7564.00 |
0.0004 |
| 392.82 |
10303.00 |
0.0004 |
| 392.84 |
520.90 |
0.0004 |
| 392.84 |
2570.00 |
0.0004 |
| 392.84 |
5129.00 |
0.0004 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 295.70 |
101.00 |
0.0001 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 101.30 |
303.15 |
0.0035 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 2 |
Temperature, K - Liquid mixture 2 |
Mole fraction of Toluene (1) - Liquid mixture 2 |
| 101.30 |
303.15 |
0.0001 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 2 |
| 273.15 |
1.50 |
0.0001 |
| 283.15 |
2.90 |
0.0001 |
| 298.15 |
7.00 |
0.0001 |
| 298.15 |
7.00 |
0.0001 |
| 305.35 |
10.20 |
0.0001 |
| 313.15 |
15.00 |
0.0001 |
| 333.15 |
38.00 |
0.0002 |
| 348.15 |
71.00 |
0.0002 |
| 373.15 |
175.00 |
0.0003 |
| 373.15 |
175.00 |
0.0003 |
| 398.15 |
383.00 |
0.0004 |
| 398.15 |
383.00 |
0.0004 |
| 413.15 |
580.00 |
0.0007 |
| 423.15 |
750.00 |
0.0008 |
| 453.15 |
1520.00 |
0.0015 |
| 458.15 |
1700.00 |
0.0017 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 273.15 |
1.50 |
0.0012 |
| 283.15 |
2.90 |
0.0017 |
| 298.15 |
7.00 |
0.0027 |
| 298.15 |
7.00 |
0.0027 |
| 305.35 |
10.20 |
0.0033 |
| 313.15 |
15.00 |
0.0043 |
| 333.15 |
38.00 |
0.0079 |
| 348.15 |
71.00 |
0.0122 |
| 373.15 |
175.00 |
0.0226 |
| 373.15 |
175.00 |
0.0239 |
| 398.15 |
383.00 |
0.0427 |
| 398.15 |
383.00 |
0.0425 |
| 413.15 |
580.00 |
0.0598 |
| 423.15 |
750.00 |
0.0692 |
| 453.15 |
1520.00 |
0.1202 |
| 458.15 |
1700.00 |
0.1328 |
Mole fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298 (Liquid mixture 1)
| Mole fraction of Water (2) - Liquid mixture 1 |
| 0.9923 |
| 0.1533 |
Mole fraction of Toluene (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298 (Liquid mixture 1)
| Mole fraction of Toluene (1) - Liquid mixture 1 |
| 0.0017 |
| 0.9570 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.15 |
0.0033 |
| 323.15 |
0.0067 |
| 373.25 |
0.0224 |
| 401.75 |
0.0410 |
| 423.45 |
0.0730 |
| 446.95 |
0.1070 |
Mole fraction of Toluene (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 298.15 |
0.0001 |
| 298.15 |
0.9970 |
| 333.15 |
0.0002 |
| 333.15 |
0.9930 |
Henry's Law constant (mole fraction scale), kPa of Toluene (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of Toluene (1) - Liquid |
| 322.00 |
85500.0 |
| 342.00 |
138800.0 |
| 362.00 |
214900.0 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0005 |
| 298.15 |
0.0009 |
| 313.15 |
0.0008 |
| 323.15 |
0.0006 |
| 323.15 |
0.0009 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 323.15 |
0.9990 |
| 313.15 |
0.9992 |
Henry's Law constant (molality scale), kPa*kg/mol of Toluene (1)
[ref]
Operational condition: Molality, mol/kg =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Toluene (1) - Liquid |
| 274.15 |
164.26 |
| 294.65 |
458.78 |
| 294.65 |
470.21 |
| 296.15 |
489.35 |
| 310.15 |
315.95 |
| 313.15 |
981.98 |
| 326.15 |
1835.68 |
| 331.15 |
3025.01 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 303.20 |
0.0013 |
| 313.20 |
0.0014 |
| 323.20 |
0.0022 |
| 333.20 |
0.0025 |
| 343.20 |
0.0050 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 303.20 |
0.9969 |
| 313.20 |
0.9958 |
| 323.20 |
0.9942 |
| 333.20 |
0.9935 |
| 343.20 |
0.9914 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 293.70 |
0.0023 |
| 303.30 |
0.0030 |
| 308.20 |
0.0032 |
| 313.50 |
0.0038 |
| 317.60 |
0.0044 |
| 324.20 |
0.0049 |
| 327.60 |
0.0055 |
| 334.10 |
0.0067 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (1) - Liquid mixture 1 |
| 297.80 |
115.00 |
0.0001 |
| 324.00 |
199.00 |
0.0001 |
| 350.60 |
197.00 |
0.0002 |
| 376.10 |
167.00 |
0.0003 |
| 401.60 |
792.00 |
0.0004 |
| 431.90 |
1261.00 |
0.0007 |
| 461.00 |
2040.00 |
0.0014 |
| 490.40 |
3800.00 |
0.0025 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.50 |
112.00 |
0.0030 |
| 324.30 |
201.00 |
0.0055 |
| 350.90 |
358.00 |
0.0115 |
| 376.60 |
478.00 |
0.0222 |
| 401.50 |
716.00 |
0.0411 |
| 431.70 |
1450.00 |
0.0779 |
| 461.80 |
3076.00 |
0.1540 |
| 491.40 |
4733.00 |
0.2520 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 299.58 |
10.20 |
| 302.58 |
11.70 |
| 307.64 |
14.10 |
| 312.66 |
17.20 |
| 322.67 |
25.50 |
| 342.71 |
56.20 |
| 352.64 |
83.30 |
| 362.71 |
121.20 |
| 372.65 |
171.50 |
| 382.73 |
239.00 |
| 392.64 |
324.70 |
| 392.88 |
327.20 |
| 397.79 |
378.40 |
| 402.34 |
431.20 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 299.58 |
10.20 |
| 302.58 |
11.70 |
| 307.64 |
14.10 |
| 312.66 |
17.20 |
| 322.67 |
25.50 |
| 342.71 |
56.20 |
| 352.64 |
83.30 |
| 362.71 |
121.20 |
| 372.65 |
171.50 |
| 382.73 |
239.00 |
| 392.64 |
324.70 |
| 392.88 |
327.20 |
| 397.79 |
378.40 |
| 402.34 |
431.20 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
1825 (Liquid)
| Temperature, K - Liquid |
Interfacial tension, N/m - Liquid |
| 383.00 |
0.0286 |
| 403.00 |
0.0264 |
| 423.00 |
0.0238 |
| 443.00 |
0.0202 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 293.20 |
0.0372 |
| 298.20 |
0.0363 |
| 303.20 |
0.0357 |
| 308.20 |
0.0352 |
| 313.20 |
0.0347 |
Interfacial tension, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 298.15 |
101.70 |
0.0362 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 293.15 |
0.0371 |
| 298.15 |
0.0361 |
| 303.15 |
0.0355 |
| 308.15 |
0.0351 |
| 313.15 |
0.0347 |
| 323.15 |
0.0343 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
1825 (Liquid)
| Temperature, K - Liquid |
Interfacial tension, N/m - Liquid |
| 383.00 |
0.0286 |
| 403.00 |
0.0264 |
| 423.00 |
0.0238 |
| 443.00 |
0.0202 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 293.20 |
0.0372 |
| 298.20 |
0.0363 |
| 303.20 |
0.0357 |
| 308.20 |
0.0352 |
| 313.20 |
0.0347 |
Interfacial tension, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 298.15 |
101.70 |
0.0362 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 293.15 |
0.0371 |
| 298.15 |
0.0361 |
| 303.15 |
0.0355 |
| 308.15 |
0.0351 |
| 313.15 |
0.0347 |
| 323.15 |
0.0343 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
| 293.20 |
998.23 |
| 298.20 |
997.06 |
| 303.20 |
995.64 |
| 308.20 |
994.04 |
| 313.20 |
992.18 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
| 293.20 |
866.83 |
| 298.20 |
862.18 |
| 303.20 |
857.53 |
| 308.20 |
852.86 |
| 313.20 |
848.13 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
| 293.20 |
998.23 |
| 298.20 |
997.06 |
| 303.20 |
995.64 |
| 308.20 |
994.04 |
| 313.20 |
992.18 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
| 293.20 |
866.83 |
| 298.20 |
862.18 |
| 303.20 |
857.53 |
| 308.20 |
852.86 |
| 313.20 |
848.13 |
Sources
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Infinite dilution activity coefficient measurements by inert gas stripping method
-
A simple apparatus for data solubility determination
-
High temperature and pressure water/oil interfacial tension benchmark data for the Ninth Industrial Fluid Properties Simulation Challenge
-
Solubility data for toluene in various aqueous alkanolamine solutions
-
Development of a Henry s constant correlation and solubility measurements of n-pentane, i-pentane, cyclopentane, n-hexane, and toluene in water
-
Interface adsorption and micelle formation of ionic liquid 1-hexyl-3-methylimidazolium chloride in the toluene + water system
-
Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
-
Liquid-Liquid Equilibrium Data, Density, Viscosity, and Interfacial Tension of Ternary System (Toluene-Acetic Acid-Water) at 298.15 K: Experiment and Correlation
-
Liquid-Liquid Equilibria for Binary Mixtures of Water + Benzene, + Toluene, and + p-Xylene from 273 K to 458 K
-
Liquid-Liquid Equilibrium for the Quaternary System Toluene + Water + Propionic Acid + Ethyl Acetate at 25 deg C and Atmospheric Pressure
-
Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
-
Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
-
Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
-
Interfacial Tension of Toluene + Water + Sodium Dodecyl Sulfate from (20 to 50) degC and pH between 4 and 9
-
Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
-
Ternary and Quaternary Liquid Liquid Equilibria for Systems of Water + Methanol + Methylanthranilate + Toluene at Different Temperatures
-
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
-
Liquid Liquid Equilibria for the Ternary System Water + Benzyl Alcohol + Methylbenzene at (303.2 to 343.2) K
-
Experimental Study of Solubility of Water in Liquid Organic Hydrogen Carriers
-
Mutual Solubility Measurements of Hydrocarbon-Water Systems Containing Benzene, Toluene, and 3-Methylpentane