Mixture of Ethanol + Tetraethyl silicate
Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Tetraethyl silicate (2)
[ref]
Fixed |
Measured |
Mole fraction of Tetraethyl silicate (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Tetraethyl silicate (2) - Gas |
0.0000 |
24.00 |
0.0000 |
0.0000 |
53.32 |
0.0000 |
0.0271 |
53.32 |
0.0105 |
0.0430 |
24.00 |
0.0101 |
0.0442 |
53.32 |
0.0115 |
0.0661 |
24.00 |
0.0106 |
0.1080 |
24.00 |
0.0118 |
0.1622 |
53.32 |
0.0144 |
0.1623 |
24.00 |
0.0168 |
0.2103 |
53.32 |
0.0175 |
0.2224 |
24.00 |
0.0199 |
0.2721 |
53.32 |
0.0205 |
0.3402 |
24.00 |
0.0260 |
0.3990 |
53.32 |
0.0257 |
0.4322 |
24.00 |
0.0323 |
0.5064 |
24.00 |
0.0395 |
0.5132 |
53.32 |
0.0352 |
0.5931 |
24.00 |
0.0511 |
0.6123 |
53.32 |
0.0477 |
0.7070 |
53.32 |
0.0590 |
0.7131 |
24.00 |
0.0753 |
0.7871 |
53.32 |
0.0880 |
0.7875 |
24.00 |
0.1080 |
0.8227 |
24.00 |
0.1311 |
0.8252 |
53.32 |
0.1170 |
0.8482 |
53.32 |
0.1352 |
0.8721 |
53.32 |
0.1721 |
0.8875 |
24.00 |
0.1973 |
0.8890 |
53.32 |
0.1910 |
0.9061 |
53.32 |
0.2211 |
0.9163 |
24.00 |
0.2494 |
0.9204 |
53.32 |
0.2474 |
0.9281 |
24.00 |
0.2745 |
0.9413 |
53.32 |
0.3430 |
0.9534 |
24.00 |
0.3713 |
0.9545 |
53.32 |
0.4018 |
0.9668 |
53.32 |
0.4953 |
0.9681 |
24.00 |
0.4670 |
0.9748 |
53.32 |
0.5482 |
0.9749 |
24.00 |
0.5202 |
0.9782 |
24.00 |
0.5541 |
0.9832 |
53.32 |
0.6650 |
0.9870 |
53.32 |
0.7011 |
0.9872 |
24.00 |
0.6830 |
0.9892 |
53.32 |
0.7370 |
0.9911 |
24.00 |
0.7533 |
0.9931 |
53.32 |
0.8152 |
0.9942 |
24.00 |
0.8214 |
0.9975 |
53.32 |
0.9222 |
0.9987 |
24.00 |
0.9121 |
1.0000 |
24.00 |
1.0000 |
1.0000 |
53.32 |
1.0000 |
Mole fraction of Tetraethyl silicate (2)
[ref]
Fixed |
Measured |
Mole fraction of Tetraethyl silicate (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Tetraethyl silicate (2) - Gas |
0.0000 |
24.00 |
0.0000 |
0.0000 |
53.32 |
0.0000 |
0.0271 |
53.32 |
0.0105 |
0.0430 |
24.00 |
0.0101 |
0.0442 |
53.32 |
0.0115 |
0.0661 |
24.00 |
0.0106 |
0.1080 |
24.00 |
0.0118 |
0.1622 |
53.32 |
0.0144 |
0.1623 |
24.00 |
0.0168 |
0.2103 |
53.32 |
0.0175 |
0.2224 |
24.00 |
0.0199 |
0.2721 |
53.32 |
0.0205 |
0.3402 |
24.00 |
0.0260 |
0.3990 |
53.32 |
0.0257 |
0.4322 |
24.00 |
0.0323 |
0.5064 |
24.00 |
0.0395 |
0.5132 |
53.32 |
0.0352 |
0.5931 |
24.00 |
0.0511 |
0.6123 |
53.32 |
0.0477 |
0.7070 |
53.32 |
0.0590 |
0.7131 |
24.00 |
0.0753 |
0.7871 |
53.32 |
0.0880 |
0.7875 |
24.00 |
0.1080 |
0.8227 |
24.00 |
0.1311 |
0.8252 |
53.32 |
0.1170 |
0.8482 |
53.32 |
0.1352 |
0.8721 |
53.32 |
0.1721 |
0.8875 |
24.00 |
0.1973 |
0.8890 |
53.32 |
0.1910 |
0.9061 |
53.32 |
0.2211 |
0.9163 |
24.00 |
0.2494 |
0.9204 |
53.32 |
0.2474 |
0.9281 |
24.00 |
0.2745 |
0.9413 |
53.32 |
0.3430 |
0.9534 |
24.00 |
0.3713 |
0.9545 |
53.32 |
0.4018 |
0.9668 |
53.32 |
0.4953 |
0.9681 |
24.00 |
0.4670 |
0.9748 |
53.32 |
0.5482 |
0.9749 |
24.00 |
0.5202 |
0.9782 |
24.00 |
0.5541 |
0.9832 |
53.32 |
0.6650 |
0.9870 |
53.32 |
0.7011 |
0.9872 |
24.00 |
0.6830 |
0.9892 |
53.32 |
0.7370 |
0.9911 |
24.00 |
0.7533 |
0.9931 |
53.32 |
0.8152 |
0.9942 |
24.00 |
0.8214 |
0.9975 |
53.32 |
0.9222 |
0.9987 |
24.00 |
0.9121 |
1.0000 |
24.00 |
1.0000 |
1.0000 |
53.32 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Tetraethyl silicate (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
24.00 |
319.50 |
0.0000 |
53.32 |
336.50 |
0.0271 |
53.32 |
336.70 |
0.0430 |
24.00 |
319.80 |
0.0442 |
53.32 |
337.10 |
0.0661 |
24.00 |
320.20 |
0.1080 |
24.00 |
321.00 |
0.1622 |
53.32 |
337.90 |
0.1623 |
24.00 |
321.80 |
0.2103 |
53.32 |
338.70 |
0.2224 |
24.00 |
323.10 |
0.2721 |
53.32 |
339.50 |
0.3402 |
24.00 |
323.90 |
0.3990 |
53.32 |
341.70 |
0.4322 |
24.00 |
325.60 |
0.5064 |
24.00 |
327.00 |
0.5132 |
53.32 |
344.40 |
0.5931 |
24.00 |
329.00 |
0.6123 |
53.32 |
346.80 |
0.7070 |
53.32 |
350.20 |
0.7131 |
24.00 |
333.10 |
0.7871 |
53.32 |
356.50 |
0.7875 |
24.00 |
338.50 |
0.8227 |
24.00 |
342.00 |
0.8252 |
53.32 |
360.80 |
0.8482 |
53.32 |
365.10 |
0.8721 |
53.32 |
369.70 |
0.8875 |
24.00 |
350.50 |
0.8890 |
53.32 |
374.00 |
0.9061 |
53.32 |
378.20 |
0.9163 |
24.00 |
355.80 |
0.9204 |
53.32 |
380.80 |
0.9281 |
24.00 |
358.50 |
0.9413 |
53.32 |
389.00 |
0.9534 |
24.00 |
366.00 |
0.9545 |
53.32 |
393.00 |
0.9668 |
53.32 |
398.70 |
0.9681 |
24.00 |
371.70 |
0.9748 |
53.32 |
401.40 |
0.9749 |
24.00 |
375.00 |
0.9782 |
24.00 |
376.60 |
0.9832 |
53.32 |
406.70 |
0.9870 |
53.32 |
408.50 |
0.9872 |
24.00 |
382.00 |
0.9892 |
53.32 |
410.00 |
0.9911 |
24.00 |
384.90 |
0.9931 |
53.32 |
413.10 |
0.9942 |
24.00 |
387.50 |
0.9975 |
53.32 |
416.50 |
0.9987 |
24.00 |
390.70 |
1.0000 |
24.00 |
393.40 |
1.0000 |
53.32 |
419.20 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Tetraethyl silicate (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
24.00 |
319.50 |
0.0000 |
53.32 |
336.50 |
0.0271 |
53.32 |
336.70 |
0.0430 |
24.00 |
319.80 |
0.0442 |
53.32 |
337.10 |
0.0661 |
24.00 |
320.20 |
0.1080 |
24.00 |
321.00 |
0.1622 |
53.32 |
337.90 |
0.1623 |
24.00 |
321.80 |
0.2103 |
53.32 |
338.70 |
0.2224 |
24.00 |
323.10 |
0.2721 |
53.32 |
339.50 |
0.3402 |
24.00 |
323.90 |
0.3990 |
53.32 |
341.70 |
0.4322 |
24.00 |
325.60 |
0.5064 |
24.00 |
327.00 |
0.5132 |
53.32 |
344.40 |
0.5931 |
24.00 |
329.00 |
0.6123 |
53.32 |
346.80 |
0.7070 |
53.32 |
350.20 |
0.7131 |
24.00 |
333.10 |
0.7871 |
53.32 |
356.50 |
0.7875 |
24.00 |
338.50 |
0.8227 |
24.00 |
342.00 |
0.8252 |
53.32 |
360.80 |
0.8482 |
53.32 |
365.10 |
0.8721 |
53.32 |
369.70 |
0.8875 |
24.00 |
350.50 |
0.8890 |
53.32 |
374.00 |
0.9061 |
53.32 |
378.20 |
0.9163 |
24.00 |
355.80 |
0.9204 |
53.32 |
380.80 |
0.9281 |
24.00 |
358.50 |
0.9413 |
53.32 |
389.00 |
0.9534 |
24.00 |
366.00 |
0.9545 |
53.32 |
393.00 |
0.9668 |
53.32 |
398.70 |
0.9681 |
24.00 |
371.70 |
0.9748 |
53.32 |
401.40 |
0.9749 |
24.00 |
375.00 |
0.9782 |
24.00 |
376.60 |
0.9832 |
53.32 |
406.70 |
0.9870 |
53.32 |
408.50 |
0.9872 |
24.00 |
382.00 |
0.9892 |
53.32 |
410.00 |
0.9911 |
24.00 |
384.90 |
0.9931 |
53.32 |
413.10 |
0.9942 |
24.00 |
387.50 |
0.9975 |
53.32 |
416.50 |
0.9987 |
24.00 |
390.70 |
1.0000 |
24.00 |
393.40 |
1.0000 |
53.32 |
419.20 |
Sources