CFD analysis of biomass gasification using downdraft gasifier

Please use this identifier to cite or link to this item: http://dspace.bits-pilani.ac.in:8080/jspui/handle/123456789/2567

Full metadata record

DC Field	Value	Language
dc.contributor.author	Sheth, P.N.	-
dc.date.accessioned	2021-10-06T09:09:07Z	-
dc.date.available	2021-10-06T09:09:07Z	-
dc.date.issued	2021	-
dc.identifier.uri	https://www.sciencedirect.com/science/article/pii/S221478532038072X	-
dc.identifier.uri	http://dspace.bits-pilani.ac.in:8080/xmlui/handle/123456789/2567	-
dc.description.abstract	CFD model has been developed for the 2D axisymmetric model of an Imbert downdraft gasifier. The present Model has been validated with experimental data. The model predicts CO, hydrogen, and CO2 with precise accuracy. Producer gas composition and gasifier temperature have been studied at different equivalence ratios (ER) i.e. 0.25 to 0.60. It is noted from the observation that the rise of the equivalence ratio tends to decrease the amount of CO, hydrogen, and methane in the producer gas whereas nitrogen and CO2 excessively increased. It has also been observed that the increase of the equivalence ratio tends to increase the temperature inside the gasifier.	en_US
dc.language.iso	en	en_US
dc.publisher	Elsiever	en_US
dc.subject	Chemical Engineering	en_US
dc.subject	Biomass	en_US
dc.subject	Gasifier	en_US
dc.subject	Syngas	en_US
dc.subject	CFD	en_US
dc.subject	DPM model	en_US
dc.title	CFD analysis of biomass gasification using downdraft gasifier	en_US
dc.type	Article	en_US
Appears in Collections:	Department of Chemical Engineering

Files in This Item:

There are no files associated with this item.