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作 者:颜学升[1] 王助良[1] 张廷发[1] 张敏[1] 孙志辉[1]
机构地区:[1]江苏大学能源与动力工程学院
出 处:《电站系统工程》2009年第6期27-30,共4页Power System Engineering
基 金:江苏省高校自然科学基金(03KJA610021)
摘 要:新型颗粒层采用固定床连续过滤、流化床连续清灰工作方式,克服了现有颗粒层过滤过程中存在的颗粒间隙增大、颗粒错位等问题,改善过滤装置的过滤性能。通过实验研究了颗粒层的清灰周期、过滤速度和过滤介质粒径等重要参数对颗粒层过滤分级效率的影响,得出了洁净气流中灰尘粒径分布规律;探讨了新型颗粒层过滤装置的低能耗、高效过滤的设计参数和运行参数。研究结果表明,选择合适粒径范围的过滤介质能达到较高的过滤效率和较低的床层阻力;调节清灰周期能灵活地改变颗粒层的过滤性能,满足各种工艺的过滤要求。Fixed bed continuous filtration and fluidized bed continuous dust removal are employed in a new granular layer, which overcomes existing problems such as increased gap among granulae and granular dislocation during filtration and improves filtration performance of the filtration device. Experiments are carried out on influences of critical parameters of dust removal cycle, filtration speed and medium dimension on filtration and classification efficiency and dust diameter distributions after filtration are obtained which is taken as a standard for judging influential extent of filtration parameters. Design and operation parameters for low energy cost and high filtration efficiency are contrastively experimented. The results indicate that with reasonable medium dimensions, higher filtration efficiency and lower bed resistance can be achieved. Filtration performance can be changed with adjustment of dust removal cycle. The adjustment makes the filtration device fulfill filtration requirements of various techniques.
分 类 号:TQ051.85[化学工程] TS176.5[轻工技术与工程—纺织材料与纺织品设计]
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