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頁籤選單縮合
題名 | Conversion of Complex Chemical Reaction in Bubbling Fluidized Beds of Fine Particles=複雜化學反應在細微粒子氣泡流體化床中之轉化率 |
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作者姓名(中文) | 呂理平; 劉淑君; | 書刊名 | Journal of the Chinese Institute of Chemical Engineers |
卷期 | 30:5 1999.09[民88.09] |
頁次 | 頁405-411 |
分類號 | 460.02 |
關鍵詞 | 複雜化學反應; 細微粒子氣泡流體化床; 轉化率; Fluidized bed reactor; Fluidization; Bubbling bed; Complex reaction; Reactor conversion; |
語文 | 英文(English) |
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 fluidized 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. |
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