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作 者:马丽萍[1] 石炎福[1] 黄卫星[1] 余华瑞[1] 祝京旭[2]
机构地区:[1]四川大学化学工程学院化学工程系,四川成都610065 [2]加拿大西安大略大学化学及生物化学工程系
出 处:《化工学报》2003年第5期619-624,共6页CIESC Journal
基 金:国家自然科学基金 (海外青年学者合作基金 )资助项目 (No 2 992 80 0 5 )~~
摘 要:用小波变换模极大值的方法对循环流化床靠近床层底部和顶部压力波动时间序列进行多重分形分析 ,确定相应的压力波动信号的间歇性指数 .结果表明循环流化床内气 固流动具有多重分形的特性 ,由间歇性参数随操作气速的变化可判断出由快速流化床向密相气力输送的改变 ,提出了新的判断循环流化床流型转变的方法 ,指出流型的转变沿提升管轴向并不是均匀一致同时改变 。The multifractal analysis for pressure fluctuation signal in bottom region and upper region of circulating fluidized bed (CFB) was performed by using the wavelet transform modulus maxima method. The intermittence index of the signals can be calculated with this method. Results show that the gas-solid flow in CFB is shown to possess a multifractal character. A new method is also proposed to identify the regime transition in CFB. The lower turning point of intermittence index curve can be used to determine the transition of flow regimes from fast fluidization to dense pneumatic conveying. The transition of flow regime in CFB is not homogeneous along the axis of riser, the transition in bottom region may be later than in upper region, and the transport velocity based on this method is also compared with that calculated by some empirical equations.
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