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Effects of shear and mixing on a continuously-fed stirred tank reactor for aerobic, biological wastewater treatment

机译:剪切和混合对连续进料搅拌釜反应器的影响,以处理好氧,生物废水

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摘要

Treatment of domestic wastewater in a 9 L well defined conventional biotechnologytype reactor was investigated over a range of stirrer speeds (8.3 to 16.7 s-1) and retentiontimes (8 to 12 h). Parameters of reactor oxygen transfer coefficient and shear werefound to be close to conditions used for pure cell culture in industrial applications ratherthan typical wastewater treatment conditions.The major treatment effects measured were carbonaceous load removal andnitrification. Carbonaceous load removal was found to be highest at low stirrer speedswith short retention times. Ammonia removal was greatest at stirrer speeds of 15 s-1with 12 h retention time. Most of the ammonia was converted to nitrite, this agreed withreports in the literature of temperature; retention time and free ammonia inhibitionpromoting nitrite build up. Specific nitrification rates of up to 35 mg(N)g-1h-1 (at 15 s-110 h retention time) were achieved in the reactor, found to be close to those observed inpure culture experiments. An inverse correlation was observed between ammonia andCBOD5 removal.The temperature increased with stirrer speed and also had a strong effect in thenitrification rate. The interaction between temperature and stirrer speed was investigatedusing a control unstirred reactor and multiple linear regression technique. It was foundthat while the temperature and stirring were correlated, separate effects could bediscerned. The stirrer effects were further investigated by varying the impeller type. Tipspeeds were matched to the disk turbine for a low and a high shear impeller. The lowershear LE20 impeller gave promising results that required a much lower power input toachieve the treatment.Finally an anoxic reactor was added to denitrify the stirred tank effluent. It was found tosuccessfully denitrify when sufficient nitrite and nitrate were supplied by the stirredtank. The combination of a stirred nitrifying tank followed by a denitrifying stage couldmake be an attractive alternative wastewater treatment method providing the stirred tankpower requirements can be reduced.
机译:在搅拌器速度(8.3至16.7 s-1)和保留时间(8至12小时)的范围内,研究了在9升定义明确的常规生物技术型反应器中处理生活废水的方法。发现反应器的氧气传递系数和剪切参数与工业应用中的纯细胞培养条件相近,而不是与典型的废水处理条件相近。所测量的主要处理效果是去除碳负载物和硝化作用。发现在低搅拌器速度下且保留时间短的情况下,碳质负载去除率最高。在搅拌速度为15 s-1且保留时间为12 h时,氨的去除效果最大。大部分氨转化为亚硝酸盐,这与温度文献中的报道一致。保留时间和游离氨的抑制作用促进亚硝酸盐的积累。在反应器中达到了高达35 mg(N)g-1h-1的特定硝化速率(在15 s-110 h的保留时间),发现该速率接近于纯培养实验中观察到的速率。氨与CBOD5的去除呈负相关。温度随着搅拌速度的增加而升高,并且对硝化速率的影响也很大。使用控制非搅拌反应器和多元线性回归技术研究温度与搅拌器速度之间的相互作用。发现虽然温度和搅拌是相关的,但是可以区分出不同的效果。通过改变叶轮类型进一步研究了搅拌器的效果。尖端速度与低和高剪切叶轮的盘式涡轮机相匹配。较低剪切的LE20叶轮产生了可喜的结果,需要更低的功率输入即可完成处理。最后,添加了一个缺氧反应器,以对搅拌的槽式废水进行反硝化。发现当搅拌罐提供足够的亚硝酸盐和硝酸盐时,反硝化成功。如果可以降低搅拌釜的功率要求,则将搅拌硝化池与反硝化步骤相结合可以成为一种有吸引力的废水处理替代方法。

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    Berry Alice L.;

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  • 年度 2002
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  • 原文格式 PDF
  • 正文语种 {"code":"en","name":"English","id":9}
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