Datasets
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Mass fraction (2)
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Tfus - Solid-liquid equilibrium temperature, K (4)
-
Vapor or sublimation pressure, kPa (2)
Mass fraction of Diisopropylamine (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Diisopropylamine (1) - Liquid mixture 1 |
303.20 |
16800.00 |
0.1000 |
308.20 |
38200.00 |
0.1000 |
313.20 |
56700.00 |
0.1000 |
316.20 |
71800.00 |
0.1000 |
303.20 |
23800.00 |
0.1500 |
305.20 |
28600.00 |
0.1500 |
308.20 |
52400.00 |
0.1500 |
310.20 |
64900.00 |
0.1500 |
313.20 |
76200.00 |
0.1500 |
316.20 |
96100.00 |
0.1500 |
303.20 |
28100.00 |
0.2000 |
305.20 |
44400.00 |
0.2000 |
308.20 |
58800.00 |
0.2000 |
310.20 |
76000.00 |
0.2000 |
313.20 |
85300.00 |
0.2000 |
316.20 |
100800.00 |
0.2000 |
303.20 |
27400.00 |
0.2500 |
305.20 |
43600.00 |
0.2500 |
308.20 |
58500.00 |
0.2500 |
310.20 |
78900.00 |
0.2500 |
313.20 |
86200.00 |
0.2500 |
316.20 |
103800.00 |
0.2500 |
303.20 |
27200.00 |
0.3000 |
305.20 |
42100.00 |
0.3000 |
308.20 |
56200.00 |
0.3000 |
310.20 |
77100.00 |
0.3000 |
313.20 |
84000.00 |
0.3000 |
316.20 |
102800.00 |
0.3000 |
303.20 |
27200.00 |
0.4000 |
305.20 |
38700.00 |
0.4000 |
308.20 |
50100.00 |
0.4000 |
310.20 |
70200.00 |
0.4000 |
313.20 |
80400.00 |
0.4000 |
316.20 |
96800.00 |
0.4000 |
303.20 |
23200.00 |
0.5000 |
305.20 |
38000.00 |
0.5000 |
308.20 |
43600.00 |
0.5000 |
310.20 |
60400.00 |
0.5000 |
313.20 |
71600.00 |
0.5000 |
316.20 |
87000.00 |
0.5000 |
303.20 |
19800.00 |
0.6000 |
305.20 |
30900.00 |
0.6000 |
308.20 |
37000.00 |
0.6000 |
310.20 |
49300.00 |
0.6000 |
313.20 |
57800.00 |
0.6000 |
316.20 |
77300.00 |
0.6000 |
303.20 |
14700.00 |
0.7000 |
305.20 |
20200.00 |
0.7000 |
308.20 |
24300.00 |
0.7000 |
310.20 |
32100.00 |
0.7000 |
313.20 |
38800.00 |
0.7000 |
316.20 |
54400.00 |
0.7000 |
303.20 |
4220.00 |
0.8000 |
305.20 |
6870.00 |
0.8000 |
308.20 |
9130.00 |
0.8000 |
310.20 |
10730.00 |
0.8000 |
313.20 |
12600.00 |
0.8000 |
316.20 |
16400.00 |
0.8000 |
Mass fraction of Diisopropylamine (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Diisopropylamine (1) - Liquid mixture 1 |
303.20 |
16800.00 |
0.1000 |
308.20 |
38200.00 |
0.1000 |
313.20 |
56700.00 |
0.1000 |
316.20 |
71800.00 |
0.1000 |
303.20 |
23800.00 |
0.1500 |
305.20 |
28600.00 |
0.1500 |
308.20 |
52400.00 |
0.1500 |
310.20 |
64900.00 |
0.1500 |
313.20 |
76200.00 |
0.1500 |
316.20 |
96100.00 |
0.1500 |
303.20 |
28100.00 |
0.2000 |
305.20 |
44400.00 |
0.2000 |
308.20 |
58800.00 |
0.2000 |
310.20 |
76000.00 |
0.2000 |
313.20 |
85300.00 |
0.2000 |
316.20 |
100800.00 |
0.2000 |
303.20 |
27400.00 |
0.2500 |
305.20 |
43600.00 |
0.2500 |
308.20 |
58500.00 |
0.2500 |
310.20 |
78900.00 |
0.2500 |
313.20 |
86200.00 |
0.2500 |
316.20 |
103800.00 |
0.2500 |
303.20 |
27200.00 |
0.3000 |
305.20 |
42100.00 |
0.3000 |
308.20 |
56200.00 |
0.3000 |
310.20 |
77100.00 |
0.3000 |
313.20 |
84000.00 |
0.3000 |
316.20 |
102800.00 |
0.3000 |
303.20 |
27200.00 |
0.4000 |
305.20 |
38700.00 |
0.4000 |
308.20 |
50100.00 |
0.4000 |
310.20 |
70200.00 |
0.4000 |
313.20 |
80400.00 |
0.4000 |
316.20 |
96800.00 |
0.4000 |
303.20 |
23200.00 |
0.5000 |
305.20 |
38000.00 |
0.5000 |
308.20 |
43600.00 |
0.5000 |
310.20 |
60400.00 |
0.5000 |
313.20 |
71600.00 |
0.5000 |
316.20 |
87000.00 |
0.5000 |
303.20 |
19800.00 |
0.6000 |
305.20 |
30900.00 |
0.6000 |
308.20 |
37000.00 |
0.6000 |
310.20 |
49300.00 |
0.6000 |
313.20 |
57800.00 |
0.6000 |
316.20 |
77300.00 |
0.6000 |
303.20 |
14700.00 |
0.7000 |
305.20 |
20200.00 |
0.7000 |
308.20 |
24300.00 |
0.7000 |
310.20 |
32100.00 |
0.7000 |
313.20 |
38800.00 |
0.7000 |
316.20 |
54400.00 |
0.7000 |
303.20 |
4220.00 |
0.8000 |
305.20 |
6870.00 |
0.8000 |
308.20 |
9130.00 |
0.8000 |
310.20 |
10730.00 |
0.8000 |
313.20 |
12600.00 |
0.8000 |
316.20 |
16400.00 |
0.8000 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Diisopropylamine (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0071 |
273.50 |
0.0148 |
271.30 |
0.0230 |
270.30 |
0.0331 |
269.30 |
0.0436 |
266.20 |
0.0548 |
264.10 |
0.0664 |
259.90 |
0.0799 |
257.70 |
1.0000 |
317.70 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Diisopropylamine (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
273.20 |
0.0069 |
272.20 |
0.0146 |
271.40 |
0.0232 |
271.00 |
0.0326 |
268.60 |
0.0435 |
266.90 |
0.0545 |
263.90 |
0.0670 |
261.60 |
0.0802 |
259.30 |
1.0000 |
315.80 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Diisopropylamine (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0071 |
273.50 |
0.0148 |
271.30 |
0.0230 |
270.30 |
0.0331 |
269.30 |
0.0436 |
266.20 |
0.0548 |
264.10 |
0.0664 |
259.90 |
0.0799 |
257.70 |
1.0000 |
317.70 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Diisopropylamine (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
273.20 |
0.0069 |
272.20 |
0.0146 |
271.40 |
0.0232 |
271.00 |
0.0326 |
268.60 |
0.0435 |
266.90 |
0.0545 |
263.90 |
0.0670 |
261.60 |
0.0802 |
259.30 |
1.0000 |
315.80 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Diisopropylamine (1) - Liquid |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.0707 |
357.30 |
53.40 |
0.0809 |
357.31 |
52.80 |
0.1009 |
357.31 |
51.80 |
0.1418 |
357.31 |
49.90 |
0.1613 |
334.59 |
18.10 |
0.1650 |
349.15 |
34.10 |
0.1707 |
334.59 |
17.80 |
0.1712 |
357.30 |
48.40 |
0.1750 |
349.15 |
33.80 |
0.2020 |
334.59 |
17.10 |
0.2029 |
357.30 |
46.80 |
0.2059 |
349.14 |
32.60 |
0.2218 |
334.60 |
16.70 |
0.2265 |
349.15 |
31.80 |
0.2417 |
334.59 |
16.20 |
0.2446 |
357.31 |
44.60 |
0.2467 |
349.15 |
31.10 |
0.2623 |
334.59 |
15.70 |
0.2680 |
349.15 |
30.20 |
0.2927 |
334.60 |
15.00 |
0.2937 |
357.30 |
41.50 |
0.2937 |
357.31 |
41.80 |
0.2987 |
349.15 |
28.90 |
0.3227 |
334.60 |
14.30 |
0.3282 |
349.15 |
27.70 |
0.3534 |
334.59 |
13.50 |
0.3591 |
349.15 |
26.40 |
0.3634 |
357.30 |
37.40 |
0.3825 |
334.60 |
12.80 |
0.3920 |
349.15 |
24.90 |
0.4036 |
357.30 |
34.80 |
0.4330 |
334.59 |
11.50 |
0.4420 |
349.16 |
22.70 |
0.4424 |
357.31 |
32.40 |
0.5039 |
334.59 |
9.80 |
0.5043 |
357.30 |
28.50 |
0.5128 |
349.14 |
19.60 |
0.5535 |
357.30 |
25.40 |
0.5558 |
334.60 |
8.60 |
0.5638 |
349.15 |
17.30 |
0.6090 |
357.30 |
21.90 |
0.6450 |
334.59 |
6.60 |
0.6502 |
349.16 |
13.80 |
0.7016 |
357.30 |
16.30 |
0.7325 |
334.59 |
4.80 |
0.7396 |
349.15 |
10.10 |
1.0000 |
334.59 |
0.00 |
1.0000 |
349.15 |
0.00 |
1.0000 |
357.28 |
0.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Diisopropylamine (1) - Liquid |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.0707 |
357.30 |
53.40 |
0.0809 |
357.31 |
52.80 |
0.1009 |
357.31 |
51.80 |
0.1418 |
357.31 |
49.90 |
0.1613 |
334.59 |
18.10 |
0.1650 |
349.15 |
34.10 |
0.1707 |
334.59 |
17.80 |
0.1712 |
357.30 |
48.40 |
0.1750 |
349.15 |
33.80 |
0.2020 |
334.59 |
17.10 |
0.2029 |
357.30 |
46.80 |
0.2059 |
349.14 |
32.60 |
0.2218 |
334.60 |
16.70 |
0.2265 |
349.15 |
31.80 |
0.2417 |
334.59 |
16.20 |
0.2446 |
357.31 |
44.60 |
0.2467 |
349.15 |
31.10 |
0.2623 |
334.59 |
15.70 |
0.2680 |
349.15 |
30.20 |
0.2927 |
334.60 |
15.00 |
0.2937 |
357.30 |
41.50 |
0.2937 |
357.31 |
41.80 |
0.2987 |
349.15 |
28.90 |
0.3227 |
334.60 |
14.30 |
0.3282 |
349.15 |
27.70 |
0.3534 |
334.59 |
13.50 |
0.3591 |
349.15 |
26.40 |
0.3634 |
357.30 |
37.40 |
0.3825 |
334.60 |
12.80 |
0.3920 |
349.15 |
24.90 |
0.4036 |
357.30 |
34.80 |
0.4330 |
334.59 |
11.50 |
0.4420 |
349.16 |
22.70 |
0.4424 |
357.31 |
32.40 |
0.5039 |
334.59 |
9.80 |
0.5043 |
357.30 |
28.50 |
0.5128 |
349.14 |
19.60 |
0.5535 |
357.30 |
25.40 |
0.5558 |
334.60 |
8.60 |
0.5638 |
349.15 |
17.30 |
0.6090 |
357.30 |
21.90 |
0.6450 |
334.59 |
6.60 |
0.6502 |
349.16 |
13.80 |
0.7016 |
357.30 |
16.30 |
0.7325 |
334.59 |
4.80 |
0.7396 |
349.15 |
10.10 |
1.0000 |
334.59 |
0.00 |
1.0000 |
349.15 |
0.00 |
1.0000 |
357.28 |
0.00 |
Sources