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http://hdl.handle.net/2080/301
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DC Field | Value | Language |
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dc.contributor.author | Singh, R K | - |
dc.date.accessioned | 2006-07-01T04:01:10Z | - |
dc.date.available | 2006-07-01T04:01:10Z | - |
dc.date.issued | 2006 | - |
dc.identifier.citation | Chemical Engineering World, Jan 2006, P 38-42 | en |
dc.identifier.uri | http://hdl.handle.net/2080/301 | - |
dc.description | Copyright of the published version belongs to Publisher | en |
dc.description.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. | en |
dc.format.extent | 120260 bytes | - |
dc.format.mimetype | application/pdf | - |
dc.language.iso | en | - |
dc.title | Hydrodynamic Studies of Gas-Solid Fluidization in Square Bed for Non-spherical Particles | en |
dc.type | Article | en |
Appears in Collections: | Journal Articles |
Files in This Item:
File | Description | Size | Format | |
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Square bed _CEW.pdf | 117.44 kB | Adobe PDF | View/Open |
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