Effects of initial static bed height on fractional conversion and bed pressure drop in tapered-in and tapered-out fluidized bed reactors
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文摘

Chemical reaction behavior is investigated in tapered-in and -out fluidized beds.

Effects of static bed height are explored on the fractional conversion and pressure drop.

Two types of chemical reaction with gas volume reduction and increase are studied.

An appropriate static bed height exists in tapered-in beds from reaction point of view.

Changes of static bed height in tapered-out bed slightly affect the fractional conversion.

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