Datasets
-
Mole fraction (4)
-
Excess molar enthalpy (molar enthalpy (2)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Binary diffusion coefficient, m2/s (2)
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Water (2) - Gas |
282.86 |
607.00 |
0.0020 |
282.99 |
1799.00 |
0.0007 |
282.99 |
3036.00 |
0.0004 |
283.03 |
4408.00 |
0.0003 |
293.10 |
558.00 |
0.0043 |
293.10 |
2991.00 |
0.0008 |
293.10 |
4810.00 |
0.0006 |
293.19 |
1828.00 |
0.0014 |
304.02 |
578.00 |
0.0079 |
304.36 |
1257.00 |
0.0037 |
304.51 |
2539.00 |
0.0019 |
304.61 |
4638.00 |
0.0011 |
313.15 |
1246.00 |
0.0061 |
313.16 |
4781.00 |
0.0018 |
313.26 |
2836.00 |
0.0028 |
313.30 |
498.00 |
0.0153 |
322.88 |
499.00 |
0.0240 |
322.93 |
3397.00 |
0.0040 |
322.93 |
4841.00 |
0.0029 |
323.10 |
1420.00 |
0.0087 |
332.45 |
1448.00 |
0.0134 |
332.52 |
461.00 |
0.0427 |
332.52 |
2454.00 |
0.0086 |
332.52 |
4358.00 |
0.0049 |
342.31 |
425.00 |
0.0719 |
342.31 |
462.00 |
0.0658 |
342.31 |
4962.00 |
0.0067 |
342.39 |
1466.00 |
0.0219 |
342.42 |
2899.00 |
0.0103 |
351.87 |
540.00 |
0.0849 |
351.92 |
2957.00 |
0.0162 |
351.95 |
4797.00 |
0.0111 |
352.12 |
1480.00 |
0.0335 |
363.00 |
555.00 |
0.1260 |
363.08 |
4874.00 |
0.0161 |
Mole fraction of Nitrogen (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Nitrogen (1) - Liquid |
274.18 |
3006.00 |
0.0005 |
274.18 |
3837.00 |
0.0006 |
274.19 |
979.00 |
0.0002 |
274.19 |
1900.00 |
0.0003 |
274.19 |
4868.00 |
0.0008 |
274.21 |
5993.00 |
0.0010 |
274.26 |
6775.00 |
0.0011 |
278.05 |
5900.00 |
0.0009 |
278.15 |
971.00 |
0.0002 |
278.16 |
4934.00 |
0.0007 |
278.17 |
6916.00 |
0.0010 |
278.19 |
2990.00 |
0.0005 |
278.19 |
3990.00 |
0.0006 |
278.21 |
1763.00 |
0.0003 |
283.12 |
1012.00 |
0.0001 |
283.13 |
2413.00 |
0.0003 |
283.13 |
4877.00 |
0.0007 |
283.16 |
7160.00 |
0.0010 |
283.18 |
5825.00 |
0.0008 |
288.09 |
2395.00 |
0.0003 |
288.11 |
966.00 |
0.0001 |
288.11 |
4042.00 |
0.0005 |
288.11 |
5444.00 |
0.0007 |
288.11 |
7003.00 |
0.0009 |
293.08 |
2511.00 |
0.0003 |
293.09 |
3964.00 |
0.0005 |
293.09 |
5655.00 |
0.0007 |
293.09 |
6945.00 |
0.0008 |
293.12 |
984.00 |
0.0001 |
298.04 |
6967.00 |
0.0007 |
298.07 |
1004.00 |
0.0001 |
298.08 |
4745.00 |
0.0005 |
298.10 |
2233.00 |
0.0003 |
298.10 |
3717.00 |
0.0004 |
308.18 |
2196.00 |
0.0002 |
308.18 |
4180.00 |
0.0004 |
308.19 |
7032.00 |
0.0007 |
308.23 |
1040.00 |
0.0001 |
323.13 |
915.00 |
0.0001 |
323.13 |
2031.00 |
0.0002 |
323.13 |
3542.00 |
0.0003 |
323.13 |
4957.00 |
0.0004 |
323.14 |
7043.00 |
0.0006 |
342.92 |
2424.00 |
0.0002 |
342.98 |
4956.00 |
0.0004 |
342.98 |
6941.00 |
0.0005 |
342.99 |
992.00 |
0.0001 |
362.90 |
1001.00 |
0.0001 |
362.90 |
1900.00 |
0.0001 |
362.92 |
4776.00 |
0.0004 |
363.00 |
3396.00 |
0.0003 |
363.02 |
6842.00 |
0.0005 |
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Water (2) - Gas |
282.86 |
607.00 |
0.0020 |
282.99 |
1799.00 |
0.0007 |
282.99 |
3036.00 |
0.0004 |
283.03 |
4408.00 |
0.0003 |
293.10 |
558.00 |
0.0043 |
293.10 |
2991.00 |
0.0008 |
293.10 |
4810.00 |
0.0006 |
293.19 |
1828.00 |
0.0014 |
304.02 |
578.00 |
0.0079 |
304.36 |
1257.00 |
0.0037 |
304.51 |
2539.00 |
0.0019 |
304.61 |
4638.00 |
0.0011 |
313.15 |
1246.00 |
0.0061 |
313.16 |
4781.00 |
0.0018 |
313.26 |
2836.00 |
0.0028 |
313.30 |
498.00 |
0.0153 |
322.88 |
499.00 |
0.0240 |
322.93 |
3397.00 |
0.0040 |
322.93 |
4841.00 |
0.0029 |
323.10 |
1420.00 |
0.0087 |
332.45 |
1448.00 |
0.0134 |
332.52 |
461.00 |
0.0427 |
332.52 |
2454.00 |
0.0086 |
332.52 |
4358.00 |
0.0049 |
342.31 |
425.00 |
0.0719 |
342.31 |
462.00 |
0.0658 |
342.31 |
4962.00 |
0.0067 |
342.39 |
1466.00 |
0.0219 |
342.42 |
2899.00 |
0.0103 |
351.87 |
540.00 |
0.0849 |
351.92 |
2957.00 |
0.0162 |
351.95 |
4797.00 |
0.0111 |
352.12 |
1480.00 |
0.0335 |
363.00 |
555.00 |
0.1260 |
363.08 |
4874.00 |
0.0161 |
Mole fraction of Nitrogen (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Nitrogen (1) - Liquid |
274.18 |
3006.00 |
0.0005 |
274.18 |
3837.00 |
0.0006 |
274.19 |
979.00 |
0.0002 |
274.19 |
1900.00 |
0.0003 |
274.19 |
4868.00 |
0.0008 |
274.21 |
5993.00 |
0.0010 |
274.26 |
6775.00 |
0.0011 |
278.05 |
5900.00 |
0.0009 |
278.15 |
971.00 |
0.0002 |
278.16 |
4934.00 |
0.0007 |
278.17 |
6916.00 |
0.0010 |
278.19 |
2990.00 |
0.0005 |
278.19 |
3990.00 |
0.0006 |
278.21 |
1763.00 |
0.0003 |
283.12 |
1012.00 |
0.0001 |
283.13 |
2413.00 |
0.0003 |
283.13 |
4877.00 |
0.0007 |
283.16 |
7160.00 |
0.0010 |
283.18 |
5825.00 |
0.0008 |
288.09 |
2395.00 |
0.0003 |
288.11 |
966.00 |
0.0001 |
288.11 |
4042.00 |
0.0005 |
288.11 |
5444.00 |
0.0007 |
288.11 |
7003.00 |
0.0009 |
293.08 |
2511.00 |
0.0003 |
293.09 |
3964.00 |
0.0005 |
293.09 |
5655.00 |
0.0007 |
293.09 |
6945.00 |
0.0008 |
293.12 |
984.00 |
0.0001 |
298.04 |
6967.00 |
0.0007 |
298.07 |
1004.00 |
0.0001 |
298.08 |
4745.00 |
0.0005 |
298.10 |
2233.00 |
0.0003 |
298.10 |
3717.00 |
0.0004 |
308.18 |
2196.00 |
0.0002 |
308.18 |
4180.00 |
0.0004 |
308.19 |
7032.00 |
0.0007 |
308.23 |
1040.00 |
0.0001 |
323.13 |
915.00 |
0.0001 |
323.13 |
2031.00 |
0.0002 |
323.13 |
3542.00 |
0.0003 |
323.13 |
4957.00 |
0.0004 |
323.14 |
7043.00 |
0.0006 |
342.92 |
2424.00 |
0.0002 |
342.98 |
4956.00 |
0.0004 |
342.98 |
6941.00 |
0.0005 |
342.99 |
992.00 |
0.0001 |
362.90 |
1001.00 |
0.0001 |
362.90 |
1900.00 |
0.0001 |
362.92 |
4776.00 |
0.0004 |
363.00 |
3396.00 |
0.0003 |
363.02 |
6842.00 |
0.0005 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Mole fraction = 0.5 (Gas)
- Pressure, kPa = 101.325 (Gas)
Temperature, K - Gas |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Gas |
373.15 |
0.0539 |
383.15 |
0.0472 |
393.15 |
0.0421 |
403.15 |
0.0373 |
413.15 |
0.0336 |
423.15 |
0.0302 |
433.15 |
0.0278 |
443.15 |
0.0251 |
453.15 |
0.0229 |
463.15 |
0.0211 |
473.15 |
0.0197 |
483.15 |
0.0180 |
493.15 |
0.0168 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Mole fraction = 0.5 (Gas)
- Pressure, kPa = 101.325 (Gas)
Temperature, K - Gas |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Gas |
373.15 |
0.0539 |
383.15 |
0.0472 |
393.15 |
0.0421 |
403.15 |
0.0373 |
413.15 |
0.0336 |
423.15 |
0.0302 |
433.15 |
0.0278 |
443.15 |
0.0251 |
453.15 |
0.0229 |
463.15 |
0.0211 |
473.15 |
0.0197 |
483.15 |
0.0180 |
493.15 |
0.0168 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.24 |
2000.00 |
0.0711 |
298.19 |
5000.00 |
0.0693 |
298.15 |
10000.00 |
0.0669 |
298.25 |
20000.00 |
0.0632 |
298.17 |
30000.00 |
0.0608 |
298.20 |
40000.00 |
0.0592 |
323.22 |
2000.00 |
0.0671 |
323.22 |
5000.00 |
0.0657 |
323.21 |
10000.00 |
0.0635 |
323.21 |
20000.00 |
0.0604 |
323.13 |
30000.00 |
0.0582 |
323.13 |
40000.00 |
0.0565 |
373.25 |
2000.00 |
0.0582 |
373.23 |
5000.00 |
0.0572 |
373.15 |
10000.00 |
0.0556 |
373.15 |
20000.00 |
0.0533 |
373.13 |
30000.00 |
0.0512 |
373.13 |
40000.00 |
0.0504 |
448.02 |
2000.00 |
0.0433 |
447.98 |
5000.00 |
0.0428 |
448.05 |
10000.00 |
0.0419 |
448.02 |
20000.00 |
0.0405 |
448.03 |
30000.00 |
0.0395 |
448.00 |
40000.00 |
0.0389 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.24 |
2000.00 |
0.0711 |
298.19 |
5000.00 |
0.0693 |
298.15 |
10000.00 |
0.0669 |
298.25 |
20000.00 |
0.0632 |
298.17 |
30000.00 |
0.0608 |
298.20 |
40000.00 |
0.0592 |
323.22 |
2000.00 |
0.0671 |
323.22 |
5000.00 |
0.0657 |
323.21 |
10000.00 |
0.0635 |
323.21 |
20000.00 |
0.0604 |
323.13 |
30000.00 |
0.0582 |
323.13 |
40000.00 |
0.0565 |
373.25 |
2000.00 |
0.0582 |
373.23 |
5000.00 |
0.0572 |
373.15 |
10000.00 |
0.0556 |
373.15 |
20000.00 |
0.0533 |
373.13 |
30000.00 |
0.0512 |
373.13 |
40000.00 |
0.0504 |
448.02 |
2000.00 |
0.0433 |
447.98 |
5000.00 |
0.0428 |
448.05 |
10000.00 |
0.0419 |
448.02 |
20000.00 |
0.0405 |
448.03 |
30000.00 |
0.0395 |
448.00 |
40000.00 |
0.0389 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Nitrogen (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0003 |
3000.00 |
292.15 |
0.0006 |
5000.00 |
292.15 |
0.0007 |
7000.00 |
292.15 |
0.0004 |
3000.00 |
302.15 |
0.0006 |
5000.00 |
302.15 |
0.0008 |
7000.00 |
302.15 |
0.0003 |
3000.00 |
307.15 |
0.0004 |
5000.00 |
307.15 |
0.0007 |
7000.00 |
307.15 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Nitrogen (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0003 |
3000.00 |
292.15 |
0.0006 |
5000.00 |
292.15 |
0.0007 |
7000.00 |
292.15 |
0.0004 |
3000.00 |
302.15 |
0.0006 |
5000.00 |
302.15 |
0.0008 |
7000.00 |
302.15 |
0.0003 |
3000.00 |
307.15 |
0.0004 |
5000.00 |
307.15 |
0.0007 |
7000.00 |
307.15 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.00 |
12000.00 |
0.0000 |
298.00 |
25000.00 |
0.0000 |
298.00 |
44600.00 |
0.0000 |
323.00 |
14600.00 |
0.0000 |
323.00 |
25100.00 |
0.0000 |
323.00 |
45000.00 |
0.0000 |
373.00 |
14800.00 |
0.0000 |
373.00 |
45000.00 |
0.0000 |
423.00 |
26900.00 |
1.0730e-08 |
423.00 |
45900.00 |
1.0420e-08 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.00 |
12000.00 |
0.0000 |
298.00 |
25000.00 |
0.0000 |
298.00 |
44600.00 |
0.0000 |
323.00 |
14600.00 |
0.0000 |
323.00 |
25100.00 |
0.0000 |
323.00 |
45000.00 |
0.0000 |
373.00 |
14800.00 |
0.0000 |
373.00 |
45000.00 |
0.0000 |
423.00 |
26900.00 |
1.0730e-08 |
423.00 |
45900.00 |
1.0420e-08 |
Sources