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用于垃圾渗滤液处理的膜生物反应器出水的臭氧化处理

Ozonation of membrane bioreactor effluent for landfill leachate treatment.

作者信息

Chaturapruek A, Visvanathan C, Ahn K H

机构信息

Environmental Engineering and Management Program, School of Environment, Resources and Development, Asian Institute of Technology, PO Box 4, Klong Luang, Pathumthani, 12120, Thailand.

出版信息

Environ Technol. 2005 Jan;26(1):65-73. doi: 10.1080/09593332608618583.

Abstract

Ozonation of leachate effluent obtained from a Membrane Bioreactor (MBR) process treating a medium-aged landfill leachate was investigated. The sequence of ammonia stripping, membrane bioreactor, and ozonation was used in the experiment. Ozonation of the MBR effluent showed reduction in Chemical Oxygen Demand (COD) and Total Organic Carbon (TOC) with an increase in five days Biochemical Oxygen Demand (BOD5) concentration. About 73% of COD could be removed at an ozone (O3) dosage of 4.2 mg O3 mg COD(-1). The biodegradability indicated by BOD5/COD ratio increased from 0.03 to 0.08 after ozonation at optimum ozone condition. While analyzing the molecular weight distribution, the fraction of molecular weight (MW) greater than 50 kDa of MBR effluent was transferred to MW 10-50 kDa (38%) at an ozone dosage of 810 mg O3. When O3 dosage was increased to 2,025 mg O3, a rapid change occurred in MW > 50 kDa fraction. This fraction was completely broken down into lower molecular weight fractions. This indicates partial degradation of landfill leachate by ozonation. The colour removal from the leachate was found to be greater than 95%. When the ozonated leachate was recirculated into the MBR system, along with an improvement in the performance of MBR, overall COD removal increased from 78% to 83%. Further, the ozone consumption decreased from 6.1 to 3.4 mg O3 mg COD(-1) removed, thus reducing the ozone requirement.

摘要

研究了对处理中年垃圾填埋场渗滤液的膜生物反应器(MBR)工艺产生的渗滤液流出物进行臭氧化处理的情况。实验采用了氨汽提、膜生物反应器和臭氧化的顺序。对MBR流出物进行臭氧化处理后,化学需氧量(COD)和总有机碳(TOC)降低,而五日生化需氧量(BOD5)浓度增加。在臭氧(O3)投加量为4.2 mg O3 mg COD(-1)时,约73%的COD可被去除。在最佳臭氧条件下进行臭氧化处理后,BOD5/COD比值所表明的生物降解性从0.03提高到了0.08。在分析分子量分布时,在臭氧投加量为810 mg O3时,MBR流出物中分子量(MW)大于50 kDa的部分转移到了MW 10 - 50 kDa(38%)。当臭氧投加量增加到2025 mg O3时,MW > 50 kDa部分发生了快速变化。该部分完全分解为较低分子量部分。这表明通过臭氧化可使垃圾填埋场渗滤液部分降解。发现渗滤液的脱色率大于95%。当将臭氧化后的渗滤液再循环到MBR系统中时,随着MBR性能的改善,总的COD去除率从78%提高到了83%。此外,臭氧消耗量从6.1降低到了3.4 mg O3 mg COD(-1)(去除的),从而降低了臭氧需求量。

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