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- W2392057929 abstract "The axial bed voidage distribution of FCC catalyst particles and the pressure fluctuation in a large two-dimensional turbulent fluidized bed(500 mm×30 mm×6000 mm) were investigated.First,according to the average bed voidage,a model of average bubble diameter was established,which was suitable for use in both bubble fluidized bed and turbulent fluidized bed.The calculation data of this model were agreed with the experimental observation on bubble diameters and with a similar trend to that of the pressure fluctuation,which could be used to predict the bed expansion with well agreement with the experimental results.Moreover,in the profile of pressure fluctuation along axial of fluidized bed,the curve was of a horizontal S type.According to the pressure fluctuation change,the bed could be divided four regions axially,which were grid region,bubble growing region,surface region and freeboard.According to the rapid change of fluctuation in the interface of dense phase and freeboard,a new method to determine the height of dense phase was developed,which was simple but had a substantial application value." @default.
- W2392057929 created "2016-06-24" @default.
- W2392057929 creator A5050079304 @default.
- W2392057929 date "2008-01-01" @default.
- W2392057929 modified "2023-09-23" @default.
- W2392057929 title "INVESTIGATION OF BUBBLE BEHAVIOR AND PRESSURE FLUCTUATION IN A TURBULENT FLUIDIZED BED" @default.
- W2392057929 hasPublicationYear "2008" @default.
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