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首页> 外文期刊>Advances in environmental research: An international journal of research in environmental science, engineering and technology >The effect of air-induced velocity gradient and dissolved oxygen on bioflocculation in the trickling filter/solids contact process
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The effect of air-induced velocity gradient and dissolved oxygen on bioflocculation in the trickling filter/solids contact process

机译:滴滤器/固体接触过程中空气诱导的速度梯度和溶解氧对生物絮凝的影响

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摘要

The trickling filter/solids contact process (TF/SC) was developed in the late 1970s to improve the final effluent quality of existing trickling filters, to be able to meet stricter effluent EPA requirements. Although the TF/SC process has been successful in achieving this goal, it is still not fully understood, and there is limited information regarding the factors affecting the flocculation phenomena occurring in the solids contact chamber (SCC), such as the effect of bubble size and dissolved oxygen on bioflocculation efficiency. To better understand the kinetics of bioflocculation in a continuous flow solids contact chamber, a long-term experimental program was conducted using a TF/SC pilot plant constructed at the Marrero, Louisiana wastewater treatment plant. This program, developed from January 1998 through October 2000, included a detailed investigation of the kinetics of the bioflocculation process taking place in the SCC. This paper deals with the effect of air-induced velocity gradient on bioflocculation. Analysis of the observed data demonstrates that excellent final effluent quality can be obtained with a wide range of air-induced velocity gradients (G) and with dissolved oxygen levels as low as 0.5 mg/1. However, from the point of view of SCC design, a value of G=25/s, achieved using a fine-bubble aeration system, and dissolved oxygen (DO) levels between 1.0 and 1.4 mg/1, are recommended to consistently produce a very good final effluent. This study also demonstrates that additional mechanical flocculation units would not be needed if a fine-bubble aeration system were used in the SCC and the floc structure could be preserved while transferring the floc from the SCC to the secondary sedimentation tank. However, considering that floc breakup frequently occurs during mixed liquor transfer from the SCC to the secondary clarifier, flocculator center wells should be used as a precaution in final clarification units to re-flocculate the mixed liquor.
机译:滴滤池/固体接触过程(TF / SC)于1970年代后期开发,旨在提高现有滴滤池的最终出水质量,从而能够满足更严格的废水EPA要求。尽管TF / SC工艺已成功实现了这一目标,但仍未完全理解,有关影响固体接触腔(SCC)中发生的絮凝现象的因素(如气泡大小的影响)的信息有限和溶解氧对生物絮凝效率的影响。为了更好地了解连续流式固体接触室中生物絮凝的动力学,使用在路易斯安那州Marrero废水处理厂建造的TF / SC中试装置进行了长期实验程序。从1998年1月到2000年10月开发的该程序包括对SCC中发生的生物絮凝过程动力学的详细研究。本文研究了空气流速梯度对生物絮凝的影响。对观测数据的分析表明,在宽范围的空气诱导的速度梯度(G)和低至0.5 mg / 1的溶解氧水平下,均可获得出色的最终废水质量。但是,从SCC设计的角度来看,建议使用细气泡曝气系统获得的G = 25 / s值以及1.0至1.4 mg / 1的溶解氧(DO)水平始终如一地产生最终废水非常好。这项研究还表明,如果在SCC中使用细气泡曝气系统,则无需额外的机械絮凝装置,并且在将絮凝物从SCC转移到二级沉淀池时,可以保留絮凝物的结构。但是,考虑到絮凝物在从SCC转移到二级澄清池的混合液中经常发生分解,因此在最终澄清池中应使用絮凝器中心孔作为预防措施,以重新絮凝混合液。

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