Dortmund Data Bank
Excess Volume 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.
Excess Volume Data Set 9414
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
| Excess Volume [cm3/mol] |
x1 [mol/mol] |
| 0.1750 |
0.04860 |
| 0.2020 |
0.06340 |
| 0.2830 |
0.10410 |
| 0.2990 |
0.11730 |
| 0.3560 |
0.16430 |
| 0.3560 |
0.16530 |
| 0.3860 |
0.19790 |
| 0.4150 |
0.21250 |
| 0.4440 |
0.24250 |
| 0.4130 |
0.80320 |
| 0.4040 |
0.81370 |
| 0.3600 |
0.83380 |
| 0.3220 |
0.87020 |
| 0.2490 |
0.90680 |
| 0.1550 |
0.94360 |
| 0.0510 |
0.98670 |
Reference
| Source |
| Blanco A.M.; Ortega J.: Experimental Study of Miscibility, Density and Isobaric Vapor-Liquid Equilibrium Values for Mixtures of Methanol in Hydrocarbons (C5, C6). Fluid Phase Equilib. 122 (1996) 207-222 |
Excess Volume Data Set 9415
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
| Excess Volume [cm3/mol] |
x1 [mol/mol] |
| 0.1970 |
0.04250 |
| 0.3980 |
0.10030 |
| 0.4810 |
0.13380 |
| 0.5760 |
0.19130 |
| 0.6380 |
0.24760 |
| 0.6780 |
0.30630 |
| 0.6950 |
0.38750 |
| 0.6930 |
0.45260 |
| 0.6760 |
0.51130 |
| 0.6510 |
0.55900 |
| 0.6310 |
0.60680 |
| 0.6050 |
0.64570 |
| 0.5570 |
0.69280 |
| 0.5130 |
0.72810 |
| 0.4430 |
0.78090 |
| 0.2950 |
0.87280 |
| 0.1380 |
0.94550 |
Reference
| Source |
| Blanco A.M.; Ortega J.: Experimental Study of Miscibility, Density and Isobaric Vapor-Liquid Equilibrium Values for Mixtures of Methanol in Hydrocarbons (C5, C6). Fluid Phase Equilib. 122 (1996) 207-222 |
Excess Volume Data Set 10893
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
| Temperature |
298.150 |
K |
| Pressure |
1.010 |
bar |
Data Table
| Excess Volume [cm3/mol] |
x1 [mol/mol] |
| 0.1640 |
0.05320 |
| 0.1830 |
0.06010 |
| 0.3270 |
0.13800 |
| 0.3410 |
0.15400 |
| 0.4510 |
0.24910 |
| 0.4490 |
0.81390 |
| 0.3950 |
0.85290 |
| 0.3730 |
0.86440 |
| 0.2830 |
0.91990 |
| 0.1830 |
0.94940 |
| 0.0910 |
0.97710 |
Reference
| Source |
| Orge B.; Iglesias M.; Rodriguez A.; Canosa J.M.; Tojo J.: Mixing Properties of (Methanol, Ethanol or 1-Propanol) with (n-Pentane, n-Hexane, n-Heptane and n-Octane) at 298.15 K. Fluid Phase Equilib. 133 (1997) 213-227 |
Diagrams
List of All References
| Source |
| Blanco A.M.; Ortega J.: Experimental Study of Miscibility, Density and Isobaric Vapor-Liquid Equilibrium Values for Mixtures of Methanol in Hydrocarbons (C5, C6). Fluid Phase Equilib. 122 (1996) 207-222 |
| Orge B.; Iglesias M.; Rodriguez A.; Canosa J.M.; Tojo J.: Mixing Properties of (Methanol, Ethanol or 1-Propanol) with (n-Pentane, n-Hexane, n-Heptane and n-Octane) at 298.15 K. Fluid Phase Equilib. 133 (1997) 213-227 |
Excess Volume Data Overview
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