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- W2384134174 abstract "Distribution law of pressure drop and particle concentration of circulating fluidized bed was studied under different operating conditions in a circulating fluidized bed experimental device with the diameter of 250mm and the height of 9000 mm and a radial non-uniformity index( RNI) was applied to describe quantitatively the non-uniformity in radial distribution of solid particle concentration along the axial. The results show that pressure balance curve of the whole loop takes the shape of 8 in circulating fluidized bed. The bed pressure drop mainly concentrates in the venturi,compared to return solids stream position in venturi expansion,the proportion of venturi pressure drop reduces. Changes of pressure drop in venturi are consistent with the main bed in the similar operating conditions. In the circulating fluidized bed particle concentration increases with increasing of solids circulating flow rate or decrease of superficial gas velocity,the radial particle concentration is a typical core-annulus pattern with a dilute center and a concentrated wall,radial average concentration in circulating fluidized bed increase and then decrease with increase of riser height,distribution of section average particle concentration is the C type along the axial. The radial non-uniformity of solid particle concentration increases firstly and then decreases up the riser,and correlate strongly with cross-sectional average solid particle concentration. The results give a good guidance to the design and optimization of the circulating fluidized bed desulfurization reactor." @default.
- W2384134174 created "2016-06-24" @default.
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- W2384134174 date "2014-01-01" @default.
- W2384134174 modified "2023-09-24" @default.
- W2384134174 title "Experimental Study on the Flow Field Characteristics in the Circulating Fluidized Bed Desulfurization Reactor" @default.
- W2384134174 hasPublicationYear "2014" @default.
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