Mixture of Phenol, 2-methoxy- + Carbon dioxide + Diethylamine, hydrochloride
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Molality, mol/kg of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Solvent: Amount ratio of component to other component of binary solvent of Phenol, 2-methoxy- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0197 |
293.15 |
3.0 |
45.10 |
0.0545 |
293.15 |
3.0 |
137.10 |
0.0892 |
293.15 |
3.0 |
222.80 |
0.1299 |
293.15 |
3.0 |
320.60 |
0.1693 |
293.15 |
3.0 |
414.90 |
0.2120 |
293.15 |
3.0 |
517.70 |
0.0199 |
303.15 |
3.0 |
53.90 |
0.0499 |
303.15 |
3.0 |
133.60 |
0.0862 |
303.15 |
3.0 |
241.50 |
0.1203 |
303.15 |
3.0 |
339.10 |
0.1525 |
303.15 |
3.0 |
428.80 |
0.1834 |
303.15 |
3.0 |
513.50 |
0.0201 |
313.15 |
3.0 |
59.20 |
0.0565 |
313.15 |
3.0 |
182.90 |
0.0840 |
313.15 |
3.0 |
271.20 |
0.1103 |
313.15 |
3.0 |
357.50 |
0.1344 |
313.15 |
3.0 |
436.40 |
0.1602 |
313.15 |
3.0 |
524.60 |
0.0160 |
323.15 |
3.0 |
56.60 |
0.0388 |
323.15 |
3.0 |
143.40 |
0.0665 |
323.15 |
3.0 |
246.00 |
0.0893 |
323.15 |
3.0 |
331.90 |
0.1154 |
323.15 |
3.0 |
428.90 |
0.1421 |
323.15 |
3.0 |
525.40 |
0.0209 |
293.15 |
4.0 |
49.60 |
0.0558 |
293.15 |
4.0 |
134.60 |
0.0936 |
293.15 |
4.0 |
224.40 |
0.1344 |
293.15 |
4.0 |
323.10 |
0.1736 |
293.15 |
4.0 |
411.30 |
0.2212 |
293.15 |
4.0 |
516.10 |
0.0233 |
303.15 |
4.0 |
61.70 |
0.0525 |
303.15 |
4.0 |
142.60 |
0.0837 |
303.15 |
4.0 |
227.50 |
0.1279 |
303.15 |
4.0 |
345.80 |
0.1577 |
303.15 |
4.0 |
425.40 |
0.1947 |
303.15 |
4.0 |
524.80 |
0.0163 |
313.15 |
4.0 |
54.20 |
0.0442 |
313.15 |
4.0 |
141.10 |
0.0759 |
313.15 |
4.0 |
242.20 |
0.1099 |
313.15 |
4.0 |
346.80 |
0.1371 |
313.15 |
4.0 |
431.80 |
0.1691 |
313.15 |
4.0 |
529.20 |
0.0156 |
323.15 |
4.0 |
58.90 |
0.0415 |
323.15 |
4.0 |
148.40 |
0.0641 |
323.15 |
4.0 |
230.10 |
0.0952 |
323.15 |
4.0 |
337.70 |
0.1217 |
323.15 |
4.0 |
430.40 |
0.1483 |
323.15 |
4.0 |
526.80 |
0.0218 |
293.15 |
5.0 |
48.80 |
0.0584 |
293.15 |
5.0 |
131.90 |
0.1077 |
293.15 |
5.0 |
245.30 |
0.1440 |
293.15 |
5.0 |
326.50 |
0.1862 |
293.15 |
5.0 |
419.20 |
0.2321 |
293.15 |
5.0 |
522.30 |
0.0220 |
303.15 |
5.0 |
57.00 |
0.0557 |
303.15 |
5.0 |
148.30 |
0.0930 |
303.15 |
5.0 |
244.90 |
0.1300 |
303.15 |
5.0 |
341.20 |
0.1629 |
303.15 |
5.0 |
424.40 |
0.1995 |
303.15 |
5.0 |
520.10 |
0.0196 |
313.15 |
5.0 |
58.80 |
0.0514 |
313.15 |
5.0 |
156.00 |
0.0904 |
313.15 |
5.0 |
273.60 |
0.1109 |
313.15 |
5.0 |
336.30 |
0.1425 |
313.15 |
5.0 |
428.60 |
0.1842 |
313.15 |
5.0 |
550.70 |
0.0166 |
323.15 |
5.0 |
59.90 |
0.0563 |
323.15 |
5.0 |
193.10 |
0.0732 |
323.15 |
5.0 |
253.30 |
0.0975 |
323.15 |
5.0 |
333.80 |
0.1270 |
323.15 |
5.0 |
431.50 |
0.1592 |
323.15 |
5.0 |
535.80 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Molality, mol/kg of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Solvent: Amount ratio of component to other component of binary solvent of Phenol, 2-methoxy- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0197 |
293.15 |
3.0 |
45.10 |
0.0545 |
293.15 |
3.0 |
137.10 |
0.0892 |
293.15 |
3.0 |
222.80 |
0.1299 |
293.15 |
3.0 |
320.60 |
0.1693 |
293.15 |
3.0 |
414.90 |
0.2120 |
293.15 |
3.0 |
517.70 |
0.0199 |
303.15 |
3.0 |
53.90 |
0.0499 |
303.15 |
3.0 |
133.60 |
0.0862 |
303.15 |
3.0 |
241.50 |
0.1203 |
303.15 |
3.0 |
339.10 |
0.1525 |
303.15 |
3.0 |
428.80 |
0.1834 |
303.15 |
3.0 |
513.50 |
0.0201 |
313.15 |
3.0 |
59.20 |
0.0565 |
313.15 |
3.0 |
182.90 |
0.0840 |
313.15 |
3.0 |
271.20 |
0.1103 |
313.15 |
3.0 |
357.50 |
0.1344 |
313.15 |
3.0 |
436.40 |
0.1602 |
313.15 |
3.0 |
524.60 |
0.0160 |
323.15 |
3.0 |
56.60 |
0.0388 |
323.15 |
3.0 |
143.40 |
0.0665 |
323.15 |
3.0 |
246.00 |
0.0893 |
323.15 |
3.0 |
331.90 |
0.1154 |
323.15 |
3.0 |
428.90 |
0.1421 |
323.15 |
3.0 |
525.40 |
0.0209 |
293.15 |
4.0 |
49.60 |
0.0558 |
293.15 |
4.0 |
134.60 |
0.0936 |
293.15 |
4.0 |
224.40 |
0.1344 |
293.15 |
4.0 |
323.10 |
0.1736 |
293.15 |
4.0 |
411.30 |
0.2212 |
293.15 |
4.0 |
516.10 |
0.0233 |
303.15 |
4.0 |
61.70 |
0.0525 |
303.15 |
4.0 |
142.60 |
0.0837 |
303.15 |
4.0 |
227.50 |
0.1279 |
303.15 |
4.0 |
345.80 |
0.1577 |
303.15 |
4.0 |
425.40 |
0.1947 |
303.15 |
4.0 |
524.80 |
0.0163 |
313.15 |
4.0 |
54.20 |
0.0442 |
313.15 |
4.0 |
141.10 |
0.0759 |
313.15 |
4.0 |
242.20 |
0.1099 |
313.15 |
4.0 |
346.80 |
0.1371 |
313.15 |
4.0 |
431.80 |
0.1691 |
313.15 |
4.0 |
529.20 |
0.0156 |
323.15 |
4.0 |
58.90 |
0.0415 |
323.15 |
4.0 |
148.40 |
0.0641 |
323.15 |
4.0 |
230.10 |
0.0952 |
323.15 |
4.0 |
337.70 |
0.1217 |
323.15 |
4.0 |
430.40 |
0.1483 |
323.15 |
4.0 |
526.80 |
0.0218 |
293.15 |
5.0 |
48.80 |
0.0584 |
293.15 |
5.0 |
131.90 |
0.1077 |
293.15 |
5.0 |
245.30 |
0.1440 |
293.15 |
5.0 |
326.50 |
0.1862 |
293.15 |
5.0 |
419.20 |
0.2321 |
293.15 |
5.0 |
522.30 |
0.0220 |
303.15 |
5.0 |
57.00 |
0.0557 |
303.15 |
5.0 |
148.30 |
0.0930 |
303.15 |
5.0 |
244.90 |
0.1300 |
303.15 |
5.0 |
341.20 |
0.1629 |
303.15 |
5.0 |
424.40 |
0.1995 |
303.15 |
5.0 |
520.10 |
0.0196 |
313.15 |
5.0 |
58.80 |
0.0514 |
313.15 |
5.0 |
156.00 |
0.0904 |
313.15 |
5.0 |
273.60 |
0.1109 |
313.15 |
5.0 |
336.30 |
0.1425 |
313.15 |
5.0 |
428.60 |
0.1842 |
313.15 |
5.0 |
550.70 |
0.0166 |
323.15 |
5.0 |
59.90 |
0.0563 |
323.15 |
5.0 |
193.10 |
0.0732 |
323.15 |
5.0 |
253.30 |
0.0975 |
323.15 |
5.0 |
333.80 |
0.1270 |
323.15 |
5.0 |
431.50 |
0.1592 |
323.15 |
5.0 |
535.80 |
Sources