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DC Field | Value | Language |
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dc.contributor.author | Desai, Parth S. | - |
dc.date.accessioned | 2014-06-24T06:12:46Z | - |
dc.date.available | 2014-06-24T06:12:46Z | - |
dc.date.issued | 2014-06-01 | - |
dc.identifier.uri | http://hdl.handle.net/123456789/4566 | - |
dc.description.abstract | Because of hiking price and depleting source of fossil fuels demand of bio-diesel increases. Hydrogen is the most energy proficient fuel nowadays and also it creates least pollutants. Glycerol is the byproduct of bio-diesel production so it is very energy proficient process when we exploit glycerol as a reactant. Steam is the best medium for reforming of biodiesel byproducts which subsuming hydrocarbons at high pressure with minimal time. Water imparts as a source to produce steam. Experiments carried out in atmospheric condition with solid-gas phase tubular reactor at a temperature ambit of about 750 ◦C to 950 ◦C. Theoretically 7 moles are obtained but practically it is hardly about 4.5 to 6 moles. This report focuses on the conversion of glycerol to hydrogen using nickel based catalyst supported on γ-Al2O3,ZSM-5 and SiO2 with different composition of nickel. | en_US |
dc.publisher | Institute of Technology | en_US |
dc.relation.ispartofseries | 12MCHC05; | - |
dc.subject | Chemical 2012 | en_US |
dc.subject | Project Report | en_US |
dc.subject | Project Report 2012 | en_US |
dc.subject | Chemical Project Report | en_US |
dc.subject | 12MCH | en_US |
dc.subject | 12MCHC | en_US |
dc.subject | 12MCHC05 | en_US |
dc.subject | CPPD | en_US |
dc.subject | CPPD 2012 | en_US |
dc.subject | Bio-diesel | en_US |
dc.subject | Glycerol | en_US |
dc.subject | Steam | en_US |
dc.subject | γ-Al2O3 | en_US |
dc.subject | ZSM-5 | en_US |
dc.subject | SiO2 | en_US |
dc.subject | Reforming | en_US |
dc.subject | Catalyst | en_US |
dc.title | Production Of Hydrogen From Glycerol Via Steam Reforming Process | en_US |
dc.type | Dissertation | en_US |
Appears in Collections: | Dissertation, CH (CPPD) |
Files in This Item:
File | Description | Size | Format | |
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12MCHC05.pdf | 12MCHC05 | 1.37 MB | Adobe PDF | ![]() View/Open |
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