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膜序批式生物反应器脱氮性能研究
摘要点击 3420  全文点击 1904  投稿时间:2007-10-26  修订日期:2007-11-29
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中文关键词  氮去除  膜序批式反应器  曝气强度  FISH-CLSM  交换比
英文关键词  nitrogen removal  membrane sequencing batch reactor  aeration strength  FISH-CLSM  volumetric exchange ratio
作者单位
张胜 北京师范大学环境学院北京100875 
张铭川 北京师范大学环境学院北京100875 
徐立荣 北京师范大学环境学院北京100875 
竺建荣 北京师范大学环境学院北京100875 
刘鸿亮 北京师范大学环境学院北京100875 
中文摘要
      采用厌-好氧交替膜序批式反应器, 实验室人工合成配水,连续运行300 d,对反应器脱氮性能进行了研究.结果表明,污泥浓度达到18 g·L-1时,污泥粒径大小在100 μm以上的占96%,污泥出现颗粒化.FISH-CLSM分析AOB及NOB的群落空间分布表明它们在污泥中大量存在. NH+4-N进水50 mg·L-1左右时出水在1 mg·L-1以下,硝化反应在180~210 min就可以完成.曝气强度与硝化反应速率密切相关,曝气强度为100 m3·(m2·h)-1时,NH+4-N降解速率最佳达24.25 mg·(L·h)-1,系统硝化性能稳定.影响系统脱氮的主要因素是反硝化速率,曝气强度为69 m3·(m2·h)-1时,对NO-3-N的利用率为10.98 mg·(L·h)-1,出水NO-3-N浓度为4.4 mg·L-1,滞留在厌氧段的浓度3.5 mg·L-1为最低,反硝化效果最好.曝气过量或不足时反硝化速率都低.在保证系统处理能力的同时,大的交换比0.35有利于系统脱氮运行.C/N比为2时,反硝化速率最高,>2时出现NO-2-N的积累.
英文摘要
      Nitrogen removal performance was investigated using synthetic wastewater as feed without sludge discharge in an anaerobic/aerobic membrane sequencing batch reactor (MSBR) during 300 days operation. The results showed that MLSS in reactor was retained up to about 18 g·L-1, sludge size larger than 100 μm was 96%, and aerobic granular sludge was developed. The bacterial community observation of AOB and NOB by FISH-CLSM for sludge revealed that they were existed in larger numbers. When influent NH+4-N concentration was about 50 mg·L-1, effluent NH+4-N concentration was lower than to 1 mg·L-1, and nitrification could complete in 180_210 min. There was a good correlation between nitrification reaction and aeration strength. When aeration strength was 100 m3·(m2·h)-1, NH+4-N degradation rate 24.25 mg·(L·h)-1, and nitrification reaction in MSBR was stable. The main factor determining nitrogen removal of the system was denitrification rate, which was optimal at aeration 69 m3·(m2·h)-1, when the nitrification rate of NO-3-N 10.98 mg·(L·h)-1, effluent NO-3-N 4.4 mg·L-1, and NO-3-N in the beginning of anaerobic phase 3.5 mg·L-1. The denitrification performance was not benefited by excessive aeration or deficient aeration. Bigger volumetric exchange ratio was helpful for nitrogen removal and the system treatment capacity. The C/N ratio 2 was suitable to good denitrification rate, while there was a NO-2-N accumulation if C/N ratio was larger than 2.

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