Please use this identifier to cite or link to this item:
http://hdl.handle.net/2080/301| Title: | Hydrodynamic Studies of Gas-Solid Fluidization in Square Bed for Non-spherical Particles |
| Authors: | Singh, R K |
| Issue Date: | 2006 |
| Citation: | Chemical Engineering World, Jan 2006, P 38-42 |
| Abstract: | Fluidization as an established fluid-solid contacting technique has found extensive applications in unit operations like drying, adsorption and in chemical processes Viz. solid-catalized reactions, carbonization, gasification and combustion. A fluidized bed can be achieved by increasing the upward velocity of the fluid through a fixed bed. Fluidized bed technique as compared to fixed bed has specific advantages. Albeit many advantages claimed of fluidization, the efficiency and the quality in large scale and deep gas-solid beds are seriously affected by bubbling, channeling and slugging behaviors, resulting in poor gas-solid contact, lower diffusion and heat transfer rates. |
| Description: | Copyright of the published version belongs to Publisher |
| URI: | http://hdl.handle.net/2080/301 |
| Appears in Collections: | Journal Articles |
Files in This Item:
| File | Description | Size | Format | |
|---|---|---|---|---|
| Square bed _CEW.pdf | 117.44 kB | Adobe PDF | View/Open |
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