| dc.contributor.author | Sheth, Pratik N. | |
| dc.date.accessioned | 2024-09-05T10:38:26Z | |
| dc.date.available | 2024-09-05T10:38:26Z | |
| 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/jspui/xmlui/handle/123456789/15466 | |
| 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 | Elsevier | 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 approach | 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 |
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