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缺氧污泥区低氧化还原电位对好氧-沉淀-缺氧活性污泥工艺中剩余污泥产量的影响。

Effect of low ORP in anoxic sludge zone on excess sludge production in oxic-settling-anoxic activated sludge process.

作者信息

Saby Sébastien, Djafer Malik, Chen Guang-Hao

机构信息

Vivendi Water Research Center, c/o HKUST, Room 3636, Annex Building, Clear Water Bay Road, Hong Kong.

出版信息

Water Res. 2003 Jan;37(1):11-20. doi: 10.1016/s0043-1354(02)00253-1.

DOI:10.1016/s0043-1354(02)00253-1
PMID:12465783
Abstract

This paper studied the effect of oxidation-reduction potential (ORP) in the anoxic sludge zone on the excess sludge production in the oxic-settling-anoxic process (OSA process), a modified activated sludge process. Two pilot-scale activated sludge systems were employed in this study: (1) an OSA process that was modified from a conventional activated sludge process by inserting a sludge holding tank or namely the "anoxic" tank in the sludge return line; and (2) a conventional process used as the reference system. Each was composed of a membrane bioreactor to serve the aeration tank and solid/liquid separator. Both systems were operated with synthetic wastewater for 9 months. During the operation, the OSA system was operated with different ORP levels (+100 to -250 mV) in its anoxic tank. It has been confirmed that the OSA system produced much less excess sludge than the reference system. A lower ORP level than +100 mV in the anoxic tank is in favor of the excess sludge reduction. When the ORP level decreased from +100 to -250 mV the sludge reduction efficiency was increased from 23% to 58%. It has also been found that the OSA system performed better than the reference system with respect to the chemical oxygen demand removal efficiency and sludge settleability. The OSA process may present a potential low-cost solution to the excess sludge problem in an activated sludge process because addition of a sludge holding tank is only needed.

摘要

本文研究了缺氧污泥区的氧化还原电位(ORP)对改良活性污泥法——好氧-沉淀-缺氧工艺(OSA工艺)中剩余污泥产量的影响。本研究采用了两个中试规模的活性污泥系统:(1)一个OSA工艺,它是通过在污泥回流管中插入一个污泥储存池即“缺氧”池,由传统活性污泥工艺改良而来;(2)一个传统工艺用作参考系统。每个系统都由一个用于曝气池和固液分离器的膜生物反应器组成。两个系统均用合成废水运行9个月。在运行过程中,OSA系统在其缺氧池中以不同的ORP水平(+100至 -250 mV)运行。已证实,OSA系统产生的剩余污泥比参考系统少得多。缺氧池中低于 +100 mV的ORP水平有利于减少剩余污泥。当ORP水平从 +100 mV降至 -250 mV时,污泥减量效率从23%提高到58%。还发现,OSA系统在化学需氧量去除效率和污泥沉降性能方面比参考系统表现更好。OSA工艺可能为活性污泥工艺中的剩余污泥问题提供一种潜在的低成本解决方案,因为仅需添加一个污泥储存池。

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