کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
243713 501934 2012 7 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Sugarcane bagasse gasification: Global reaction mechanism of syngas evolution
موضوعات مرتبط
مهندسی و علوم پایه مهندسی انرژی مهندسی انرژی و فناوری های برق
پیش نمایش صفحه اول مقاله
Sugarcane bagasse gasification: Global reaction mechanism of syngas evolution
چکیده انگلیسی

Steam gasification of sugarcane bagasse has been investigated. A semi batch reactor with a fixed amount of sugarcane bagasse sample placed in steady flow of high temperature steam at atmospheric pressure has been used. The gasification of bagasse was examined at reactor and steam temperatures of 800, 900 and 1000 °C. The evolution of syngas flow rate and chemical composition has been monitored. The evolution of chemical composition and total flow rate of the syngas has been used to formulate a global reaction mechanism. The mechanism combines pyrolysis reaction mechanisms from the literature and steam gasification/reforming reactions. Steam gasification steps include steam–hydrocarbons reforming, char gasification and water gas shift reactions. Evidence of fragmentation, secondary ring opening reactions and tertiary reactions resulting in formation of gaseous hydrocarbons is supported by higher flow rates of syngas and hydrogen at high heating rates and high reactor temperatures. Increase in carbon monoxide flow rate at the expense of carbon dioxide flow rate with the increase in reactor temperature has been observed. This increase in the ratio of CO/CO2 flow rate confirms the production of CO and CO2 from the competing reaction routes. At 1000 °C gasification a total merging between the pyrolysis step and the char gasification step has been observed. This is attributed to acceleration of char gasification reactions and acceleration of steam–hydrocarbons reforming reactions. These hydrocarbons are the precursors to char formation by aromatization and repolymerization.


► Gasification of sugarcane bagasse has been investigated using a semi batch reactor.
► Global reaction mechanism combining pyrolysis and gasification reactions is presented.
► High flow rates of syngas supported fragmentation and secondary reactions.
► CO flow rate increased at higher heating rates at the expense of CO2 production.
► At high temperatures merger between pyrolysis and char gasification occurs.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Applied Energy - Volume 91, Issue 1, March 2012, Pages 75–81
نویسندگان
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