Datasets
-
Mole fraction (4)
-
Binary diffusion coefficient, m2/s (2)
Mole fraction of Nitrous oxide (1)
[ref]
Operational condition: Mole fraction =
0 (Gas)
| Fixed |
Measured |
| Temperature, K - Liquid |
Solvent: Amount concentration (molarity), mol/dm3 of Piperazine (2) - Liquid |
Mole fraction of Nitrous oxide (1) - Liquid |
| 293.15 |
0.2190 |
0.6780 |
| 293.15 |
0.5890 |
0.6690 |
| 293.15 |
0.8350 |
0.6740 |
| 293.15 |
0.9700 |
0.6620 |
| 293.15 |
1.365 |
0.6370 |
| 293.15 |
1.472 |
0.6370 |
| 298.15 |
0.2190 |
0.5900 |
| 298.15 |
0.5890 |
0.5880 |
| 298.15 |
0.8350 |
0.5910 |
| 298.15 |
0.9700 |
0.5840 |
| 298.15 |
1.365 |
0.5650 |
| 298.15 |
1.472 |
0.5640 |
| 298.15 |
1.799 |
0.5500 |
| 303.15 |
0.2190 |
0.5290 |
| 303.15 |
0.5890 |
0.5220 |
| 303.15 |
0.8350 |
0.5250 |
| 303.15 |
0.9700 |
0.5200 |
| 303.15 |
1.365 |
0.5010 |
| 303.15 |
1.472 |
0.5050 |
| 303.15 |
1.799 |
0.4920 |
| 313.15 |
0.2190 |
0.4230 |
| 313.15 |
0.5890 |
0.4240 |
| 313.15 |
0.8350 |
0.4250 |
| 313.15 |
0.9700 |
0.4240 |
| 313.15 |
1.365 |
0.4100 |
| 313.15 |
1.472 |
0.4170 |
| 313.15 |
1.799 |
0.4090 |
| 323.15 |
0.2190 |
0.3540 |
| 323.15 |
0.5890 |
0.3580 |
| 323.15 |
0.8350 |
0.3550 |
| 323.15 |
0.9700 |
0.3580 |
| 323.15 |
1.365 |
0.3500 |
| 323.15 |
1.472 |
0.3550 |
| 323.15 |
1.799 |
0.3510 |
Mass fraction of Nitrous oxide (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa of Nitrous oxide (1) - Gas |
Solvent: Mole fraction of Piperazine (2) - Liquid |
Mass fraction of Nitrous oxide (1) - Liquid |
| 293.15 |
48.90 |
0.0018 |
0.0006 |
| 293.15 |
59.40 |
0.0074 |
0.0007 |
| 293.15 |
70.60 |
0.0211 |
0.0008 |
| 293.15 |
80.30 |
0.0000 |
0.0010 |
| 293.15 |
151.30 |
0.0130 |
0.0018 |
| 298.15 |
61.20 |
0.0074 |
0.0006 |
| 298.15 |
64.00 |
0.0018 |
0.0007 |
| 298.15 |
70.90 |
0.0000 |
0.0007 |
| 298.15 |
79.10 |
0.0211 |
0.0008 |
| 303.15 |
78.30 |
0.0000 |
0.0007 |
| 303.15 |
78.90 |
0.0211 |
0.0007 |
| 303.15 |
80.80 |
0.0074 |
0.0007 |
| 303.15 |
86.30 |
0.0018 |
0.0008 |
| 303.15 |
167.20 |
0.0130 |
0.0016 |
| 313.15 |
78.30 |
0.0074 |
0.0006 |
| 313.15 |
88.70 |
0.0000 |
0.0006 |
| 313.15 |
89.70 |
0.0211 |
0.0006 |
| 313.15 |
97.10 |
0.0018 |
0.0007 |
| 313.15 |
182.30 |
0.0130 |
0.0013 |
| 323.15 |
88.80 |
0.0018 |
0.0005 |
| 323.15 |
92.70 |
0.0000 |
0.0006 |
| 323.15 |
92.70 |
0.0074 |
0.0005 |
| 323.15 |
94.30 |
0.0211 |
0.0005 |
| 323.15 |
196.40 |
0.0130 |
0.0011 |
Mole fraction of Nitrous oxide (1)
[ref]
Operational condition: Mole fraction =
0 (Gas)
| Fixed |
Measured |
| Temperature, K - Liquid |
Solvent: Amount concentration (molarity), mol/dm3 of Piperazine (2) - Liquid |
Mole fraction of Nitrous oxide (1) - Liquid |
| 293.15 |
0.2190 |
0.6780 |
| 293.15 |
0.5890 |
0.6690 |
| 293.15 |
0.8350 |
0.6740 |
| 293.15 |
0.9700 |
0.6620 |
| 293.15 |
1.365 |
0.6370 |
| 293.15 |
1.472 |
0.6370 |
| 298.15 |
0.2190 |
0.5900 |
| 298.15 |
0.5890 |
0.5880 |
| 298.15 |
0.8350 |
0.5910 |
| 298.15 |
0.9700 |
0.5840 |
| 298.15 |
1.365 |
0.5650 |
| 298.15 |
1.472 |
0.5640 |
| 298.15 |
1.799 |
0.5500 |
| 303.15 |
0.2190 |
0.5290 |
| 303.15 |
0.5890 |
0.5220 |
| 303.15 |
0.8350 |
0.5250 |
| 303.15 |
0.9700 |
0.5200 |
| 303.15 |
1.365 |
0.5010 |
| 303.15 |
1.472 |
0.5050 |
| 303.15 |
1.799 |
0.4920 |
| 313.15 |
0.2190 |
0.4230 |
| 313.15 |
0.5890 |
0.4240 |
| 313.15 |
0.8350 |
0.4250 |
| 313.15 |
0.9700 |
0.4240 |
| 313.15 |
1.365 |
0.4100 |
| 313.15 |
1.472 |
0.4170 |
| 313.15 |
1.799 |
0.4090 |
| 323.15 |
0.2190 |
0.3540 |
| 323.15 |
0.5890 |
0.3580 |
| 323.15 |
0.8350 |
0.3550 |
| 323.15 |
0.9700 |
0.3580 |
| 323.15 |
1.365 |
0.3500 |
| 323.15 |
1.472 |
0.3550 |
| 323.15 |
1.799 |
0.3510 |
Mass fraction of Nitrous oxide (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa of Nitrous oxide (1) - Gas |
Solvent: Mole fraction of Piperazine (2) - Liquid |
Mass fraction of Nitrous oxide (1) - Liquid |
| 293.15 |
48.90 |
0.0018 |
0.0006 |
| 293.15 |
59.40 |
0.0074 |
0.0007 |
| 293.15 |
70.60 |
0.0211 |
0.0008 |
| 293.15 |
80.30 |
0.0000 |
0.0010 |
| 293.15 |
151.30 |
0.0130 |
0.0018 |
| 298.15 |
61.20 |
0.0074 |
0.0006 |
| 298.15 |
64.00 |
0.0018 |
0.0007 |
| 298.15 |
70.90 |
0.0000 |
0.0007 |
| 298.15 |
79.10 |
0.0211 |
0.0008 |
| 303.15 |
78.30 |
0.0000 |
0.0007 |
| 303.15 |
78.90 |
0.0211 |
0.0007 |
| 303.15 |
80.80 |
0.0074 |
0.0007 |
| 303.15 |
86.30 |
0.0018 |
0.0008 |
| 303.15 |
167.20 |
0.0130 |
0.0016 |
| 313.15 |
78.30 |
0.0074 |
0.0006 |
| 313.15 |
88.70 |
0.0000 |
0.0006 |
| 313.15 |
89.70 |
0.0211 |
0.0006 |
| 313.15 |
97.10 |
0.0018 |
0.0007 |
| 313.15 |
182.30 |
0.0130 |
0.0013 |
| 323.15 |
88.80 |
0.0018 |
0.0005 |
| 323.15 |
92.70 |
0.0000 |
0.0006 |
| 323.15 |
92.70 |
0.0074 |
0.0005 |
| 323.15 |
94.30 |
0.0211 |
0.0005 |
| 323.15 |
196.40 |
0.0130 |
0.0011 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Fixed |
Measured |
| Molality, mol/kg of Piperazine (2) - Liquid |
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
| 0.2950 |
293.15 |
0.0000 |
| 0.2950 |
298.15 |
0.0000 |
| 0.2950 |
303.15 |
0.0000 |
| 0.2950 |
313.15 |
0.0000 |
| 0.2950 |
323.15 |
0.0000 |
| 0.2950 |
333.15 |
0.0000 |
| 0.6290 |
293.15 |
0.0000 |
| 0.6290 |
298.15 |
0.0000 |
| 0.6290 |
303.15 |
0.0000 |
| 0.6290 |
313.15 |
0.0000 |
| 0.6290 |
323.15 |
0.0000 |
| 0.6290 |
333.15 |
0.0000 |
| 1.067 |
293.15 |
0.0000 |
| 1.067 |
298.15 |
0.0000 |
| 1.067 |
303.15 |
0.0000 |
| 1.067 |
313.15 |
0.0000 |
| 1.067 |
323.15 |
0.0000 |
| 1.067 |
333.15 |
0.0000 |
| 1.368 |
293.15 |
0.0000 |
| 1.368 |
298.15 |
0.0000 |
| 1.368 |
303.15 |
0.0000 |
| 1.368 |
313.15 |
0.0000 |
| 1.368 |
323.15 |
0.0000 |
| 1.368 |
333.15 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Fixed |
Measured |
| Molality, mol/kg of Piperazine (2) - Liquid |
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
| 0.2950 |
293.15 |
0.0000 |
| 0.2950 |
298.15 |
0.0000 |
| 0.2950 |
303.15 |
0.0000 |
| 0.2950 |
313.15 |
0.0000 |
| 0.2950 |
323.15 |
0.0000 |
| 0.2950 |
333.15 |
0.0000 |
| 0.6290 |
293.15 |
0.0000 |
| 0.6290 |
298.15 |
0.0000 |
| 0.6290 |
303.15 |
0.0000 |
| 0.6290 |
313.15 |
0.0000 |
| 0.6290 |
323.15 |
0.0000 |
| 0.6290 |
333.15 |
0.0000 |
| 1.067 |
293.15 |
0.0000 |
| 1.067 |
298.15 |
0.0000 |
| 1.067 |
303.15 |
0.0000 |
| 1.067 |
313.15 |
0.0000 |
| 1.067 |
323.15 |
0.0000 |
| 1.067 |
333.15 |
0.0000 |
| 1.368 |
293.15 |
0.0000 |
| 1.368 |
298.15 |
0.0000 |
| 1.368 |
303.15 |
0.0000 |
| 1.368 |
313.15 |
0.0000 |
| 1.368 |
323.15 |
0.0000 |
| 1.368 |
333.15 |
0.0000 |
Sources
Note: These property values are available through the Cheméo API. A free account gives you an access key.