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Please use this identifier to cite or link to this item: http://dspace.bits-pilani.ac.in:8080/jspui/handle/123456789/15466
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dc.contributor.authorSheth, Pratik N.-
dc.date.accessioned2024-09-05T10:38:26Z-
dc.date.available2024-09-05T10:38:26Z-
dc.date.issued2021-
dc.identifier.urihttps://www.sciencedirect.com/science/article/pii/S221478532038072X-
dc.identifier.urihttp://dspace.bits-pilani.ac.in:8080/jspui/xmlui/handle/123456789/15466-
dc.description.abstractCFD 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.isoenen_US
dc.publisherElsevieren_US
dc.subjectChemical Engineeringen_US
dc.subjectBiomassen_US
dc.subjectGasifieren_US
dc.subjectSyngasen_US
dc.subjectCFD approachen_US
dc.subjectDPM modelen_US
dc.titleCFD analysis of biomass gasification using downdraft gasifieren_US
dc.typeArticleen_US
Appears in Collections:Department of Chemical Engineering

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