Zhang Ning-Bo, Li Xiang, Huang Yong, Zhang Wen-Jing
School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China.
Instatute of Environmental Biotechnology, Suzhou University of Science and Technology, Suzhou 215009, China.
Huan Jing Ke Xue. 2017 Sep 8;38(9):3793-3800. doi: 10.13227/j.hjkx.201703032.
We studied the inoculation of activated sludge from domestic sewage treatment plants. The reaction of reducing nitrate by zero-valent iron was started in the up-flow anaerobic reactor. After 52 d of operation, a nitrogen removal rate of 29.3 g·(m·d) was achieved. Ferric iron and iron oxide coated on the sludge formed in the operation process caused the mineralization and slowly decreased the sludge activity. The methods of the "supplement and replacement of the sludge in the reactor" and "changing the reflux mode of the reactor" were applied. Using the method of the supplement and replacement of the sludge in the reactor, by discharging a part of the sludge in the reactor and adding the extra dosage from the anaerobic denitrifying sludge for the treatment of wastewater, after 22 d of operation, the conversion rate of nitrate-nitrogen was 33.0 g·(m·d) and the concentration of nitrite-nitrogen was 16.50 mg·L. The effluent average concentration of ammonia-nitrogen decreased from 12.38 mg·L to 3.58 mg·L and the nitrogen removal rate was recovered from 9.9 g·(m·d)to 15.0 g·(m·d). The biological reaction weakened the chemical reduction of nitrate by zero-valent iron. Using the method of changing the reflux mode of the reactor, the reflux tank was arranged outside the reaction column using hydraulic circulation. The increase in the erosion of the upper layer of the sedimentation tank would bring out ferric iron and iron oxide with the outflow water and they would be deposited in the reflux tank. The corresponding ferric iron of transformation of nitrate settled in the external reflux tank was 58% at the ascending velocity of 3.49 m·h. The nitrate-nitrogen conversion rate was 34.3 g·(m·d), the effluent concentration of nitrite-nitrogen was 0.22 mg·L, and ammonia-nitrogen was 0.75 mg·L. Ammonia and nitrite did not extensively accumulate. The nitrogen removal rate was 33.4 g·(m·d), which solved the problem of the mineralized sludge in the long-term reactor operation. In summary, the method of reforming the reflux mode of the reactor performed better than the method of the supplement and replacement of sludge in the reactor.
我们研究了来自生活污水处理厂的活性污泥接种情况。零价铁还原硝酸盐的反应在升流式厌氧反应器中启动。运行52天后,实现了29.3 g·(m·d)的脱氮率。运行过程中在污泥上形成的铁离子和氧化铁涂层导致了污泥的矿化,并使污泥活性逐渐降低。采用了“反应器内污泥补充与置换”和“改变反应器回流模式”的方法。采用反应器内污泥补充与置换的方法,通过排出反应器内部分污泥并添加额外剂量的厌氧反硝化污泥用于废水处理,运行22天后,硝酸盐氮转化率为33.0 g·(m·d),亚硝酸盐氮浓度为16.50 mg·L。出水氨氮平均浓度从12.38 mg·L降至3.58 mg·L,脱氮率从9.9 g·(m·d)恢复至15.0 g·(m·d)。生物反应削弱了零价铁对硝酸盐的化学还原作用。采用改变反应器回流模式的方法,利用水力循环将回流罐设置在反应柱外部。沉淀池上层侵蚀的增加会使铁离子和氧化铁随出水带出并沉积在回流罐中。在上升流速为3.49 m·h时,外部回流罐中硝酸盐转化对应的铁离子沉降率为58%。硝酸盐氮转化率为34.3 g·(m·d),出水亚硝酸盐氮浓度为0.22 mg·L,氨氮为0.75 mg·L。氨和亚硝酸盐没有大量积累。脱氮率为33.4 g·(m·d),解决了反应器长期运行中污泥矿化的问题。综上所述,改变反应器回流模式的方法比反应器内污泥补充与置换的方法效果更好。