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A+OSA污泥减量工艺碳元素平衡与减量机制研究
摘要点击 1677  全文点击 1113  投稿时间:2011-09-04  修订日期:2011-11-17
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中文关键词  污泥减量  碳平衡  OSA工艺  污泥衰减  水解发酵
英文关键词  sludge reduction  carbon balance  oxic-settling-anaerobic (OSA)  sludge decay  hydrolysis fermentation
作者单位E-mail
翟小敏 重庆大学城市建设与环境工程学院,三峡库区生态环境教育部重点实验室,重庆 400045 zxmgreen@163.com 
高旭 重庆大学城市建设与环境工程学院,三峡库区生态环境教育部重点实验室,重庆 400045 gaoxu@cqu.edu.cn 
张曼曼 安徽省建设工程勘察设计院,合肥 230001  
贾丽 重庆大学城市建设与环境工程学院,三峡库区生态环境教育部重点实验室,重庆 400045  
郭劲松 重庆大学城市建设与环境工程学院,三峡库区生态环境教育部重点实验室,重庆 400045  
中文摘要
      为深入研究OSA工艺减量途径,揭示其污泥减量机制,对缺氧-好氧-沉淀-厌氧(A+OSA)污泥减量系统和AO参照系统进行碳元素平衡分析,以考察贮泥池插入对减量系统的影响; 辨识两系统各单元碳元素在固液气三相间的迁移转化途径,推测减量驱动机制.碳平衡结果表明,在贮泥池停留时间7.14 h时,碳元素在减量系统剩余污泥中的比例比参照系统高约50%,与减量系统达到49.98%的污泥减量效果相对应.贮泥池的插入能有效减少污泥产量.各单元碳元素变化量表明,减量系统缺氧池与好氧池(主体反应区)用于生物合成的碳元素量高于参照系统; 贮泥池中污泥出现负增长,且释放CH4量较主体反应区有大幅增加.DGGE图谱证实了贮泥池中存在与污泥衰减有关的水解发酵型细菌.A+OSA工艺污泥减量是贮泥池污泥衰减和主体反应区补偿性增长共同作用的结果.
英文摘要
      In order to deeply explore the mechanism of sludge reduction in OSA system, carbon balance was performed in an anoxic-oxic-settling-anaerobic(A+OSA) system and a reference AO system to investigate effects of inserting a sludge holding tank in sludge cycle line on the sludge reduction process. Meanwhile, carbon mass change in each reaction unit was identified in terms of solid, liquid and gas phases. The causes of excess sludge reduction in A+OSA system were deduced. The carbon balance results show that when the hydraulic retention time in the sludge holding tank is 7.14 h, carbon percent in solid phase of the sludge reduction system is nearly 50% higher than that of the reference system, supporting the consequence that sludge reduction rate of 49.98% had been achieved. The insertion of a sludge holding tank in the sludge return circuit can be effective in sludge reduction. Carbon changes in each unit reveal that the amount of carbon consumed for biosynthesis in the anoxic and oxic tanks (main reaction zone) of the sludge reduction system is higher than in that of the reference system. Sludge decay is observed in the sludge holding tank. Furthermore, CH4 released from the sludge holding tank is significantly higher than that from the main reaction zone. The DGGE profiles show that there are hydrolytic-fermentative bacteria in the sludge holding tank related to sludge decay. The excess sludge reduction in the A+OSA system could be a result of the combination of sludge decay in the sludge holding tank and sludge compensatory growth in the main reaction cell.

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