• 作者： Leu, Lii-Ping; Liu, Shu-Chun
• 中文摘要： 依據Kunii-Levenspiel模式吾人導出一階可逆複雜化學反應在細微粒子氣泡流體化床中之轉化率及產品分佈。並導出氣泡大小對轉化率之影響。在氣泡流體化床中較小之氣泡有較高之轉化率。依據 Kunii-Levenspiel模式氣泡流體化床中之轉化率較活塞式及混流式反應器為低。
• 英文摘要： Based on the Kunii-Levenspiel model, the conversion and product distribution equations are developed for the network complex first order reversible chemical reaction in fluidezed beds of fine particles. The influence of the bubble diameter on the conversion is shown. The smaller size bubble results in a higher conversion in the fluidized bed reactors. The Kunii-Levenspiel model predicts a lower conversion of bubbling fluidized bed reactors comparing to plug flow and backmix flow reactors.
• 中文關鍵字： 流體化床反應器; 流體化; 氣泡床; 複雜反應; 反應器轉化率
• 英文關鍵字： Fluidized Bed Reactor; Fluidization; Bubbling Bed; Complex Reaction; Reactor Conversion