Dortmund Data Bank
Vapor-Liquid Equilibrium Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Vapor-Liquid Equilibrium Data Set 12361
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
1544.420 |
0.12700 |
0.86000 |
3013.006 |
0.26800 |
0.91900 |
4067.906 |
0.37800 |
0.93900 |
5102.114 |
0.52400 |
0.94900 |
6212.169 |
0.69300 |
0.95900 |
8446.079 |
0.95400 |
0.97300 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Thies M.C.: Vapor- Liquid Equilibrium of Model Coal-derived Compounds with Methanol at Elevated Temperatures and Pressures. Thesis (1985) |
Vapor-Liquid Equilibrium Data Set 12362
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
1978.797 |
0.12000 |
0.81700 |
3275.011 |
0.21200 |
0.88000 |
4826.323 |
0.34100 |
0.90300 |
5874.330 |
0.43100 |
0.92000 |
6929.230 |
0.52900 |
0.92200 |
8032.393 |
0.62600 |
0.92700 |
9273.437 |
0.74500 |
0.93000 |
10362.814 |
0.83300 |
0.91200 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Thies M.C.: Vapor- Liquid Equilibrium of Model Coal-derived Compounds with Methanol at Elevated Temperatures and Pressures. Thesis (1985) |
Vapor-Liquid Equilibrium Data Set 12363
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C10H8 |
128.174 |
91-20-3 |
Naphthalene |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
2240.789 |
0.11000 |
0.72400 |
3716.268 |
0.19800 |
0.81500 |
5115.900 |
0.28700 |
0.85200 |
6088.073 |
0.34800 |
0.86800 |
6722.380 |
0.39000 |
0.87400 |
7984.130 |
0.46500 |
0.88700 |
9549.228 |
0.58400 |
0.88500 |
11741.768 |
0.74300 |
0.84600 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Thies M.C.: Vapor- Liquid Equilibrium of Model Coal-derived Compounds with Methanol at Elevated Temperatures and Pressures. Thesis (1985) |
Diagrams
List of All References
Source |
Thies M.C.: Vapor- Liquid Equilibrium of Model Coal-derived Compounds with Methanol at Elevated Temperatures and Pressures. Thesis (1985) |
Vapor-Liquid Equilibrium Data Overview
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