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三相生物流化床的相含率及气液传质性能研究

Study on the Phase Holdup and Gas-Liquid Mass Transfer Efficiency in Biological Fluidised Bed

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【作者】 谢澄陈中豪疏明君李友明

【Author】 XIE Cheng ,CHEN Zhong-hao ,SHU Ming-jun ,LI You-ming(Paper Making &Pollution Control Engineering Research Center,South Chi na University of Technology,Guangzhou 510641,China)

【机构】 华南理工大学造纸与污染控制国家工程研究中心华南理工大学造纸与污染控制国家工程研究中心 广东广州510641广东广州510641广东广州510641

【摘要】 采用内循环三相生物流化床,用清水进行了在不同活性炭载体加入量下,当进气量改变时流化床内的气液传质性能的实验,认为当Ug≥0.75m3/h时,随着气体流量增加,可改善流化床的氧传质效率,缩短循环时间和混合时间,提高气含率,但过高的气体流量(Ug≥1.1m3/h)并不利于流化床的操作。载体加入量增加,会导致氧传递性能下降,循环时间和混合时间缩短,气含率减小。

【Abstract】 Gas-liquid mass transfer efficiency test with tap water and varied activ ated carbon carrier addition at varying amount of inlet a ir in an internal recycle three-phase biological fluidized bed shows that when U g ≥0.75m 3 /h,the oxygen transfer efficiency in t he fluidized bed can be improved,the circulating time as well as the mixing time can be reduced,and th e air content can be increased with th e increase of air flow,while too high an air flow(U g ≥1.1m 3 /h)is unfavorable to the operation of th e fluidized bed.Increase of carrier addition will result in the decreased oxygen transfer eff iciency,shortened recycle time,mi xing time as well as the decrease of air con-tent.

  • 【文献出处】 工业用水与废水 ,Industrial Water & Wastewater , 编辑部邮箱 ,2001年06期
  • 【分类号】X703.1
  • 【被引频次】19
  • 【下载频次】189
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