Please use this identifier to cite or link to this item: http://13.232.72.61:8080/jspui/handle/123456789/581
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dc.contributor.authorShauka, S. Shahid-
dc.date.accessioned2018-12-08T11:33:42Z-
dc.date.available2018-12-08T11:33:42Z-
dc.date.issued2011-07-
dc.identifier.citationShauka, S. Shahid. (2011). Progress in biomass and bioenergy production. Retrieved from www.intechopen.comen_US
dc.identifier.isbn978-953-307-491-7-
dc.identifier.urihttps://www.intechopen.com/books/progress-in-biomass-and-bioenergy-production.-
dc.identifier.urihttp://13.232.72.61:8080/jspui/handle/123456789/581-
dc.description.abstractIn this chapter we are introducing the research of particles hydrodynamics in a cold flow model of Fast Internal Circulating Fluidized Bed (FICFB) biomass gasification process and its scale-up to industrial pilot plant. A laboratory unit has been made for the purposes of experimental research. The laboratory unit is three times smaller than the later pilot plant. For a reliable observation of the flow process, similar flow conditions must be created in the laboratory unit and the pilot plant. The results of the laboratory model will be similar to those of the actual device if geometry, flow and Reynolds numbers are the same. Therefore, there is no need to bring a full-scale gasificator into the laboratory and actually test it. This is an example of "dynamic similarity".en_US
dc.language.isoenen_US
dc.publisherInTechen_US
dc.subjectBiotechnologyen_US
dc.subjectChemistryen_US
dc.subjectBioenergyen_US
dc.subjectBiomassen_US
dc.titleProgress in Biomass and Bioenergy Production.en_US
dc.typeBooken_US
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