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http://nopr.niscpr.res.in/handle/123456789/26463Full metadata record
| DC Field | Value | Language |
|---|---|---|
| dc.contributor.author | Rahman, A N E | - |
| dc.contributor.author | Akmal, M A Khaleel | - |
| dc.contributor.author | Prasad, K B S | - |
| dc.date.accessioned | 2014-02-10T06:19:34Z | - |
| dc.date.available | 2014-02-10T06:19:34Z | - |
| dc.date.issued | 2001-01 | - |
| dc.identifier.issn | 0975-1084 (Online); 0022-4456 (Print) | - |
| dc.identifier.uri | http://hdl.handle.net/123456789/26463 | - |
| dc.description | 52-59 | en_US |
| dc.description.abstract | Pyrolysis of solid wastes like papers, rags, garden wastes, used tea leaves and municipal solid waste (MSW) is carried out in a fixed bed reactor for studying distribution of energy in pyrolytic products and their possible applications as fuel. Pyrolysis is conducted between 450°C to 650°C and at different reaction times. The temperature of 600°C is found to be good forgetting maximum yield of tar and is enhanced from 16 per cent to 27.6 per cent as the pyrolysis time reduces from 35 min to 5 min. The average yield of char and gas is found between 30-34 per cent and 16-20 per cent respectively, irrespective of reaction time. The calorific values of solid, liquid and gaseous products of pyrolysis of all the wastes show a good fuel potential. The tar can be used as furnace oil, char can be utilized as a feedstock for producing active carbon and gas as a fuel for industrial furnaces or internal combustion engines. | en_US |
| dc.language.iso | en_US | en_US |
| dc.publisher | NISCAIR-CSIR, India | en_US |
| dc.rights | CC Attribution-Noncommercial-No Derivative Works 2.5 India | en_US |
| dc.source | JSIR Vol.60(01) [January 2001] | en_US |
| dc.title | Pyrolysis of Solid Wastes | en_US |
| dc.type | Article | en_US |
| Appears in Collections: | JSIR Vol.60(01) [January 2001] | |
Files in This Item:
| File | Description | Size | Format | |
|---|---|---|---|---|
| JSIR 60(1) 52-59.pdf | 1.06 MB | Adobe PDF | View/Open |
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