Marangoni convection and mass transfer from the liquid to the gas phase under microgravity conditions
β Scribed by J. H. Lichtenbelt; A. A. H. Drinkenburg; H. A. Dijkstra
- Book ID
- 104742884
- Publisher
- Springer
- Year
- 1986
- Tongue
- English
- Weight
- 401 KB
- Volume
- 73
- Category
- Article
- ISSN
- 0028-1042
No coin nor oath required. For personal study only.
β¦ Synopsis
p , urification processes, like distillation, adsorp- tion and desorption, are of great importance in chemical engineering. In most systems compounds are transferred between two immiscible liquids or between a liquid and a gas. The flow directions of the two phases can be co-current, crosscurrent or counter-current, the counter-current process having the highest efficiency. Where possible, this last process is used in industry, for instance in spray towers, plate columns and packed columns. A packed column is a hollow, vertical cylinder filled with particles, which can be of any shape. In a transfer process, involving a liquid and a gas, the liquid flows downward over the packing in the shape of films, rivulets and droplets. The function of the packing material is to create a large contact area between the two fluids. The degree of performance of the transfer process can be expressed by the quantity Nog, i.e. the number of the transfer units. In a packed column Nog is proportional to the product of the mass transfer coefficient K and the contact area A.
π SIMILAR VOLUMES
## Av =103fO denommator m their rate equation also mvolves the same factor Equabon (4) reqrures a further expressIon for the forward velocity v:-= whrch can be deduced by Langmuir-Hmshelwood kmetlcs or other appropnate assumptrons We gave such a derivahon eqmvalent the case where Steps 2 and 3 m e