The Gas and Solid Exchanges between Both Areas of Fluidized Bed Used for Coal Gasification
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摘要: 本工作在三區流化床粉煤氣化的基礎上,對雙區流化床粉煤氣化區間氣、固摻混進行了冷態研究。實驗結果表明,三區流化床改為雙區方案是可行的,在原三區的基礎上適當提高流化指數可滿足燃燒區和氣化區熱交換的要求,且能減少煤氣和煙氣的摻混;分區流化床粉煤氣化以薄料層操作,有助于提高煤氣的發熱值;此外,還考察了床內縱向構件和固體粒度分布對區間氣體摻混的影響,床內縱向構件可減少兩區的氣體摻混,進一步提高煤氣的發熱值。Abstract: Based on the fluidized bed divided into three areas, the exchanges of gas and solid between the both areas of fluidized bed were studied through a cold model. Experiments showed that it is feasible to reform three areas in fluidized bed to both areas, which is helpful to operating and decreasing the investment of fluidized bed. If fluidization index is properly raised, the heat exchange between combustion and gasification areas will meet the needs of operating, and the heat value of gas will also increase. A vertical device in fluidized bed will help to increase the heat value of gas.
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Key words:
- fluidized bed /
- coal gasification
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