Dortmund Data Bank
G-function (G-G0)/T of Ethanol
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.
Component
| Formula |
Molar Mass |
CAS Registry Number |
Name |
| C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of Ethanol
Diagrams
Data Table
| T [K] |
G-function (G-G0)/T [J/(mol*K)] |
State |
Reference |
| 100.00 |
-186.92 |
Vapor |
4 |
| 150.00 |
-202.85 |
Vapor |
4 |
| 200.00 |
-214.78 |
Vapor |
4 |
| 273.15 |
-228.62 |
Vapor |
4 |
| 273.16 |
-230.96 |
Vapor |
1 |
| 298.15 |
-232.74 |
Vapor |
4 |
| 298.16 |
-235.02 |
Vapor |
1 |
| 298.16 |
-234.14 |
Vapor |
5 |
| 298.16 |
-227.07 |
Vapor |
2 |
| 298.20 |
-231.84 |
Vapor |
6 |
| 300.00 |
-235.31 |
Vapor |
1 |
| 300.00 |
-234.39 |
Vapor |
5 |
| 300.00 |
-233.03 |
Vapor |
4 |
| 300.00 |
-232.17 |
Vapor |
6 |
| 300.00 |
-226.94 |
Vapor |
2 |
| 350.00 |
-239.37 |
Vapor |
6 |
| 400.00 |
-249.91 |
Vapor |
1 |
| 400.00 |
-249.45 |
Vapor |
5 |
| 400.00 |
-247.66 |
Vapor |
4 |
| 400.00 |
-246.77 |
Vapor |
6 |
| 400.00 |
-243.13 |
Vapor |
2 |
| 450.00 |
-253.09 |
Vapor |
6 |
| 500.00 |
-262.55 |
Vapor |
1 |
| 500.00 |
-262.25 |
Vapor |
5 |
| 500.00 |
-260.51 |
Vapor |
4 |
| 500.00 |
-259.45 |
Vapor |
6 |
| 500.00 |
-256.98 |
Vapor |
2 |
| 550.00 |
-265.64 |
Vapor |
6 |
| 600.00 |
-274.43 |
Vapor |
1 |
| 600.00 |
-274.01 |
Vapor |
5 |
| 600.00 |
-272.26 |
Vapor |
4 |
| 600.00 |
-271.75 |
Vapor |
6 |
| 600.00 |
-269.58 |
Vapor |
2 |
| 700.00 |
-285.35 |
Vapor |
1 |
| 700.00 |
-285.18 |
Vapor |
5 |
| 700.00 |
-283.34 |
Vapor |
6 |
| 700.00 |
-283.24 |
Vapor |
4 |
| 700.00 |
-281.25 |
Vapor |
2 |
| 800.00 |
-295.68 |
Vapor |
1 |
| 800.00 |
-295.52 |
Vapor |
5 |
| 800.00 |
-293.88 |
Vapor |
6 |
| 800.00 |
-293.59 |
Vapor |
4 |
| 800.00 |
-292.21 |
Vapor |
2 |
| 900.00 |
-305.43 |
Vapor |
1 |
| 900.00 |
-305.39 |
Vapor |
5 |
| 900.00 |
-304.93 |
Vapor |
6 |
| 900.00 |
-303.42 |
Vapor |
4 |
| 900.00 |
-302.55 |
Vapor |
2 |
| 1000.00 |
-314.85 |
Vapor |
5 |
| 1000.00 |
-314.80 |
Vapor |
1 |
| 1000.00 |
-314.09 |
Vapor |
6 |
| 1000.00 |
-312.80 |
Vapor |
4 |
| 1000.00 |
-309.83 |
Vapor |
2 |
| 1100.00 |
-321.77 |
Vapor |
4 |
| 1100.00 |
-321.67 |
Vapor |
2 |
| 1200.00 |
-330.62 |
Vapor |
2 |
| 1200.00 |
-330.36 |
Vapor |
4 |
| 1300.00 |
-339.20 |
Vapor |
2 |
| 1300.00 |
-338.63 |
Vapor |
4 |
| 1400.00 |
-347.40 |
Vapor |
2 |
| 1400.00 |
-346.58 |
Vapor |
4 |
| 1500.00 |
-355.31 |
Vapor |
2 |
| 1500.00 |
-354.25 |
Vapor |
4 |
List of References
| Number |
Source |
| 1 |
Green J.H.S.: Thermodynamic properties of the normal alcohols C1-C12.. J.Appl.Chem. 11 (1961) 397-404 |
| 2 |
Brickwedde F.G.; Moskow M.; Aston J.G.: Equilibrium Constants of some Reactions Involved in the Production Of1,3-Butadiene.. J.Res. NBS 37 (1946) 263-279 |
| 3 |
Green J.H.S.: Thermodynamic Properties of Organic Oxygen Compounds. Part 5.-Ethyl alcohol.. Trans.Faraday Soc. 57 (1961) 2132-2137 |
| 4 |
Chao J.; Hall K.R.; Marsh K.N.; Wilhoit R.C.: Part 2. Ideal Gas Properties. J.Phys.Chem.Ref.Data 15 (1986) 1369-1436 |
| 5 |
Chermin H.A.G.: Part 28. Gaseous Normal Alcohols. Petrol.Refiner 40 (1961) 127-130 |
| 6 |
Aston J.G.: Sources of Thermodynamic Data. Methods of Application to the Industry. Ind.Eng.Chem. Ind.Ed. 34 (1942) 514-521 |
Pure Component Data Overview
© DDBST GmbH
