Vapor-liquid Equilibrium
for o-Xylene/m-Xylene
P = 26.66 kPa |
BP
Temp.
°C |
% by mole m-xylene |
| liquid |
vapor |
| 100.1 |
0.0 |
0.0 |
| 99.8 |
4.7 |
5.6 |
| 99.6 |
9.7 |
11.4 |
| 99.2 |
17.8 |
20.6 |
| 98.8 |
25.9 |
29.3 |
| 98.4 |
34.1 |
38.1 |
| 97.9 |
42.5 |
46.8 |
| 97.6 |
49.6 |
53.9 |
| 97.2 |
57.4 |
61.5 |
| 96.8 |
65.5 |
69.2 |
| 96.5 |
73.5 |
76.5 |
| 96.1 |
80.8 |
83.2 |
| 95.8 |
88.6 |
90.2 |
| 95.6 |
93.7 |
94.6 |
| 95.3 |
100.0 |
100.0 |
|
|
Vapor-liquid Equilibrium
for o-Xylene/Carbon tetrachloride
P = 760 mm Hg |
BP
Temp.
°C |
% by mole carbon tetrachloride |
| liquid |
vapor |
| 142.0 |
1.8 |
6.5 |
| 136.0 |
6.4 |
22.9 |
| 130.4 |
11.2 |
36.9 |
| 125.0 |
16.1 |
49.4 |
| 120.7 |
20.4 |
57.3 |
| 116.1 |
25.3 |
64.6 |
| 111.8 |
30.2 |
70.9 |
| 107.9 |
35.2 |
75.9 |
| 104.2 |
40.4 |
80.3 |
| 104.1 |
40.5 |
80.5 |
| 99.4 |
47.8 |
85.2 |
| 95.1 |
55.4 |
88.9 |
| 91.6 |
62.4 |
91.6 |
| 88.2 |
70.0 |
94.0 |
| 85.3 |
77.1 |
95.8 |
| 82.6 |
84.1 |
97.2 |
| 80.0 |
91.0 |
98.5 |
| 77.7 |
97.6 |
99.6 |
|
|
Vapor-liquid Equilibrium
for o-Xylene/Ethanol
P = 101.3 kPa |
BP
Temp.
°C |
% by mole ethanol |
| liquid |
vapor |
| 78.3 |
99.52 |
99.66 |
| 78.7 |
98.59 |
99.03 |
| 78.7 |
97.73 |
98.52 |
| 79.0 |
95.78 |
97.40 |
| 79.3 |
90.59 |
95.09 |
| 79.7 |
86.79 |
94.16 |
| 80.0 |
85.01 |
93.70 |
| 80.2 |
80.91 |
92.91 |
| 80.3 |
76.77 |
92.36 |
| 82.0 |
67.69 |
91.21 |
| 83.8 |
48.66 |
89.25 |
| 88.1 |
25.11 |
87.32 |
| 97.3 |
10.94 |
81.49 |
| 112.8 |
5.22 |
65.91 |
| 137.3 |
0.65 |
22.90 |
|
|
Vapor-liquid Equilibrium
for o-Xylene/Methanol
P = 101.3 kPa |
BP
Temp.
°C |
% by mole Methanol |
| liquid |
vapor |
| 64.7 |
98.78 |
99.10 |
| 64.8 |
98.33 |
98.81 |
| 64.8 |
97.67 |
98.45 |
| 64.9 |
96.70 |
97.96 |
| 65.3 |
93.34 |
96.82 |
| 65.7 |
86.84 |
95.68 |
| 66.3 |
84.24 |
95.31 |
| 66.7 |
83.30 |
95.65 |
| 67.3 |
76.74 |
94.97 |
| 68.4 |
49.33 |
94.52 |
| 71.5 |
21.76 |
93.84 |
| 102.1 |
2.49 |
80.00 |
|