Mixture of Diisopropyl ether + Furan, 2,5-dimethyl-
Datasets
-
Mole fraction (2)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Diisopropyl ether (1)
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Diisopropyl ether (1) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0500 |
50.00 |
0.1210 |
0.0960 |
50.00 |
0.2130 |
0.1340 |
50.00 |
0.2850 |
0.1790 |
50.00 |
0.3570 |
0.2310 |
50.00 |
0.4340 |
0.3350 |
50.00 |
0.5610 |
0.3960 |
50.00 |
0.6230 |
0.4450 |
50.00 |
0.6690 |
0.4990 |
50.00 |
0.7140 |
0.5530 |
50.00 |
0.7550 |
0.6010 |
50.00 |
0.7890 |
0.6460 |
50.00 |
0.8170 |
0.7500 |
50.00 |
0.8800 |
0.8100 |
50.00 |
0.9120 |
0.8690 |
50.00 |
0.9410 |
0.9300 |
50.00 |
0.9700 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
75.00 |
0.0000 |
0.0510 |
75.00 |
0.1150 |
0.0970 |
75.00 |
0.2140 |
0.1390 |
75.00 |
0.2870 |
0.1850 |
75.00 |
0.3580 |
0.2270 |
75.00 |
0.4170 |
0.2740 |
75.00 |
0.4780 |
0.3290 |
75.00 |
0.5350 |
0.3960 |
75.00 |
0.6140 |
0.4430 |
75.00 |
0.6620 |
0.4960 |
75.00 |
0.7020 |
0.5510 |
75.00 |
0.7450 |
0.6010 |
75.00 |
0.7840 |
0.6490 |
75.00 |
0.8130 |
0.7550 |
75.00 |
0.8780 |
0.8090 |
75.00 |
0.9080 |
0.8700 |
75.00 |
0.9390 |
0.9310 |
75.00 |
0.9690 |
1.0000 |
75.00 |
1.0000 |
0.0000 |
94.00 |
0.0000 |
0.0460 |
94.00 |
0.1030 |
0.0960 |
94.00 |
0.2030 |
0.1330 |
94.00 |
0.2720 |
0.1820 |
94.00 |
0.3460 |
0.2300 |
94.00 |
0.4140 |
0.2730 |
94.00 |
0.4670 |
0.2950 |
94.00 |
0.4930 |
0.3250 |
94.00 |
0.5330 |
0.3940 |
94.00 |
0.6040 |
0.4410 |
94.00 |
0.6540 |
0.4960 |
94.00 |
0.7000 |
0.5500 |
94.00 |
0.7360 |
0.5960 |
94.00 |
0.7710 |
0.6490 |
94.00 |
0.8090 |
0.7040 |
94.00 |
0.8450 |
0.7510 |
94.00 |
0.8720 |
0.8060 |
94.00 |
0.9030 |
0.8700 |
94.00 |
0.9370 |
0.9310 |
94.00 |
0.9680 |
1.0000 |
94.00 |
1.0000 |
Mole fraction of Diisopropyl ether (1)
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Diisopropyl ether (1) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0500 |
50.00 |
0.1210 |
0.0960 |
50.00 |
0.2130 |
0.1340 |
50.00 |
0.2850 |
0.1790 |
50.00 |
0.3570 |
0.2310 |
50.00 |
0.4340 |
0.3350 |
50.00 |
0.5610 |
0.3960 |
50.00 |
0.6230 |
0.4450 |
50.00 |
0.6690 |
0.4990 |
50.00 |
0.7140 |
0.5530 |
50.00 |
0.7550 |
0.6010 |
50.00 |
0.7890 |
0.6460 |
50.00 |
0.8170 |
0.7500 |
50.00 |
0.8800 |
0.8100 |
50.00 |
0.9120 |
0.8690 |
50.00 |
0.9410 |
0.9300 |
50.00 |
0.9700 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
75.00 |
0.0000 |
0.0510 |
75.00 |
0.1150 |
0.0970 |
75.00 |
0.2140 |
0.1390 |
75.00 |
0.2870 |
0.1850 |
75.00 |
0.3580 |
0.2270 |
75.00 |
0.4170 |
0.2740 |
75.00 |
0.4780 |
0.3290 |
75.00 |
0.5350 |
0.3960 |
75.00 |
0.6140 |
0.4430 |
75.00 |
0.6620 |
0.4960 |
75.00 |
0.7020 |
0.5510 |
75.00 |
0.7450 |
0.6010 |
75.00 |
0.7840 |
0.6490 |
75.00 |
0.8130 |
0.7550 |
75.00 |
0.8780 |
0.8090 |
75.00 |
0.9080 |
0.8700 |
75.00 |
0.9390 |
0.9310 |
75.00 |
0.9690 |
1.0000 |
75.00 |
1.0000 |
0.0000 |
94.00 |
0.0000 |
0.0460 |
94.00 |
0.1030 |
0.0960 |
94.00 |
0.2030 |
0.1330 |
94.00 |
0.2720 |
0.1820 |
94.00 |
0.3460 |
0.2300 |
94.00 |
0.4140 |
0.2730 |
94.00 |
0.4670 |
0.2950 |
94.00 |
0.4930 |
0.3250 |
94.00 |
0.5330 |
0.3940 |
94.00 |
0.6040 |
0.4410 |
94.00 |
0.6540 |
0.4960 |
94.00 |
0.7000 |
0.5500 |
94.00 |
0.7360 |
0.5960 |
94.00 |
0.7710 |
0.6490 |
94.00 |
0.8090 |
0.7040 |
94.00 |
0.8450 |
0.7510 |
94.00 |
0.8720 |
0.8060 |
94.00 |
0.9030 |
0.8700 |
94.00 |
0.9370 |
0.9310 |
94.00 |
0.9680 |
1.0000 |
94.00 |
1.0000 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Diisopropyl ether (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0263 |
283.15 |
0.0670 |
0.0248 |
283.15 |
0.1120 |
0.0243 |
283.15 |
0.2340 |
0.0233 |
283.15 |
0.3230 |
0.0226 |
283.15 |
0.4200 |
0.0219 |
283.15 |
0.5200 |
0.0213 |
283.15 |
0.6260 |
0.0209 |
283.15 |
1.0000 |
0.0189 |
330.15 |
0.0000 |
0.0206 |
330.15 |
0.1530 |
0.0193 |
330.15 |
0.1920 |
0.0189 |
330.15 |
0.2450 |
0.0183 |
330.15 |
0.3420 |
0.0177 |
330.15 |
0.4340 |
0.0170 |
330.15 |
0.5430 |
0.0165 |
330.15 |
0.6640 |
0.0158 |
330.15 |
0.7820 |
0.0152 |
330.15 |
0.8970 |
0.0146 |
330.15 |
1.0000 |
0.0139 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Diisopropyl ether (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0263 |
283.15 |
0.0670 |
0.0248 |
283.15 |
0.1120 |
0.0243 |
283.15 |
0.2340 |
0.0233 |
283.15 |
0.3230 |
0.0226 |
283.15 |
0.4200 |
0.0219 |
283.15 |
0.5200 |
0.0213 |
283.15 |
0.6260 |
0.0209 |
283.15 |
1.0000 |
0.0189 |
330.15 |
0.0000 |
0.0206 |
330.15 |
0.1530 |
0.0193 |
330.15 |
0.1920 |
0.0189 |
330.15 |
0.2450 |
0.0183 |
330.15 |
0.3420 |
0.0177 |
330.15 |
0.4340 |
0.0170 |
330.15 |
0.5430 |
0.0165 |
330.15 |
0.6640 |
0.0158 |
330.15 |
0.7820 |
0.0152 |
330.15 |
0.8970 |
0.0146 |
330.15 |
1.0000 |
0.0139 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
50.00 |
345.24 |
0.0500 |
50.00 |
343.13 |
0.0960 |
50.00 |
341.34 |
0.1340 |
50.00 |
339.86 |
0.1790 |
50.00 |
338.32 |
0.2310 |
50.00 |
336.70 |
0.3350 |
50.00 |
333.69 |
0.3960 |
50.00 |
332.03 |
0.4450 |
50.00 |
330.95 |
0.4990 |
50.00 |
329.69 |
0.5530 |
50.00 |
328.63 |
0.6010 |
50.00 |
327.52 |
0.6460 |
50.00 |
326.78 |
0.7500 |
50.00 |
324.85 |
0.8100 |
50.00 |
323.80 |
0.8690 |
50.00 |
322.85 |
0.9300 |
50.00 |
321.82 |
1.0000 |
50.00 |
321.03 |
0.0000 |
75.00 |
357.21 |
0.0510 |
75.00 |
355.03 |
0.0970 |
75.00 |
353.00 |
0.1390 |
75.00 |
351.47 |
0.1850 |
75.00 |
349.93 |
0.2270 |
75.00 |
348.62 |
0.2740 |
75.00 |
347.19 |
0.3290 |
75.00 |
345.78 |
0.3960 |
75.00 |
343.67 |
0.4430 |
75.00 |
342.62 |
0.4960 |
75.00 |
341.54 |
0.5510 |
75.00 |
340.22 |
0.6010 |
75.00 |
338.83 |
0.6490 |
75.00 |
338.38 |
0.7550 |
75.00 |
336.00 |
0.8090 |
75.00 |
335.23 |
0.8700 |
75.00 |
334.17 |
0.9310 |
75.00 |
333.37 |
1.0000 |
75.00 |
332.65 |
0.0000 |
94.00 |
364.37 |
0.0460 |
94.00 |
362.32 |
0.0960 |
94.00 |
360.27 |
0.1330 |
94.00 |
358.83 |
0.1820 |
94.00 |
357.17 |
0.2300 |
94.00 |
355.55 |
0.2730 |
94.00 |
354.36 |
0.2950 |
94.00 |
353.55 |
0.3250 |
94.00 |
352.64 |
0.3940 |
94.00 |
350.69 |
0.4410 |
94.00 |
349.47 |
0.4960 |
94.00 |
348.22 |
0.5500 |
94.00 |
347.38 |
0.5960 |
94.00 |
346.27 |
0.6490 |
94.00 |
345.25 |
0.7040 |
94.00 |
344.00 |
0.7510 |
94.00 |
343.28 |
0.8060 |
94.00 |
342.32 |
0.8700 |
94.00 |
341.09 |
0.9310 |
94.00 |
340.13 |
1.0000 |
94.00 |
339.57 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
50.00 |
345.24 |
0.0500 |
50.00 |
343.13 |
0.0960 |
50.00 |
341.34 |
0.1340 |
50.00 |
339.86 |
0.1790 |
50.00 |
338.32 |
0.2310 |
50.00 |
336.70 |
0.3350 |
50.00 |
333.69 |
0.3960 |
50.00 |
332.03 |
0.4450 |
50.00 |
330.95 |
0.4990 |
50.00 |
329.69 |
0.5530 |
50.00 |
328.63 |
0.6010 |
50.00 |
327.52 |
0.6460 |
50.00 |
326.78 |
0.7500 |
50.00 |
324.85 |
0.8100 |
50.00 |
323.80 |
0.8690 |
50.00 |
322.85 |
0.9300 |
50.00 |
321.82 |
1.0000 |
50.00 |
321.03 |
0.0000 |
75.00 |
357.21 |
0.0510 |
75.00 |
355.03 |
0.0970 |
75.00 |
353.00 |
0.1390 |
75.00 |
351.47 |
0.1850 |
75.00 |
349.93 |
0.2270 |
75.00 |
348.62 |
0.2740 |
75.00 |
347.19 |
0.3290 |
75.00 |
345.78 |
0.3960 |
75.00 |
343.67 |
0.4430 |
75.00 |
342.62 |
0.4960 |
75.00 |
341.54 |
0.5510 |
75.00 |
340.22 |
0.6010 |
75.00 |
338.83 |
0.6490 |
75.00 |
338.38 |
0.7550 |
75.00 |
336.00 |
0.8090 |
75.00 |
335.23 |
0.8700 |
75.00 |
334.17 |
0.9310 |
75.00 |
333.37 |
1.0000 |
75.00 |
332.65 |
0.0000 |
94.00 |
364.37 |
0.0460 |
94.00 |
362.32 |
0.0960 |
94.00 |
360.27 |
0.1330 |
94.00 |
358.83 |
0.1820 |
94.00 |
357.17 |
0.2300 |
94.00 |
355.55 |
0.2730 |
94.00 |
354.36 |
0.2950 |
94.00 |
353.55 |
0.3250 |
94.00 |
352.64 |
0.3940 |
94.00 |
350.69 |
0.4410 |
94.00 |
349.47 |
0.4960 |
94.00 |
348.22 |
0.5500 |
94.00 |
347.38 |
0.5960 |
94.00 |
346.27 |
0.6490 |
94.00 |
345.25 |
0.7040 |
94.00 |
344.00 |
0.7510 |
94.00 |
343.28 |
0.8060 |
94.00 |
342.32 |
0.8700 |
94.00 |
341.09 |
0.9310 |
94.00 |
340.13 |
1.0000 |
94.00 |
339.57 |
Sources