Fang H H P, Lau I W C, Wang P
Centre for Environmental Engineering Research, Department of Civil Engineering, The University of Hong Kong, Pokfulam Road, Hong Kong SAR, China.
Water Sci Technol. 2005;52(10-11):41-9.
Landfill leachate of Hong Kong was first treated by the upflow anaerobic sludge blanket (UASB) process. At 37 degrees C, pH 7.1-8.5 and a HRT of 5.1-6.6 days, the process removed 66-90% of COD in the leachate for loading rates of 1-2.4 g-COD/l day depending on the strength of landfill leachate. The final effluent contained 1440-1910 mg-COD/l and 70-91 mg-BOD/l. About 92.5% of the total COD removed was converted to methane and the rest was converted to biomass with an average net growth yield of 0.053 g-VSS/g-COD-removed. The granules developed in the UASB reactor were 0.5-1.5 mm in size and exhibited good settleability. The UASB effluent was then further polished by two oxidation processes. The UASB-ozonation process removed 93.0% of the 12900 mg/l of COD from the raw leachate. The UASB-Fenton-ozonation process improved the COD removal efficiency to 99.3%. The final effluent had only 85 mg/l of COD and 10 mg/l of BOD5. Ozonation was most effectively conducted at pH 7-8 with the addition of 300 mg/l of H2O2 and for the duration of 30 min. Ozonation also significantly improved the biodegradability of the organic residues. Nearly 50% of these residues could be used as carbon source in denitrification.
香港的垃圾渗滤液首先采用上流式厌氧污泥床(UASB)工艺进行处理。在37摄氏度、pH值为7.1 - 8.5且水力停留时间为5.1 - 6.6天的条件下,该工艺根据垃圾渗滤液的强度,对于1 - 2.4克化学需氧量/升·天的负荷率,去除了渗滤液中66 - 90%的化学需氧量。最终出水的化学需氧量含量为1440 - 1910毫克/升,生化需氧量含量为70 - 91毫克/升。去除的总化学需氧量中约92.5%转化为甲烷,其余转化为生物质,平均净生长产率为0.053克挥发性悬浮固体/克去除的化学需氧量。UASB反应器中形成的颗粒尺寸为0.5 - 1.5毫米,沉降性能良好。然后,UASB出水通过两种氧化工艺进一步净化。UASB - 臭氧氧化工艺去除了原渗滤液中12900毫克/升化学需氧量的93.0%。UASB - 芬顿 - 臭氧氧化工艺将化学需氧量去除效率提高到了99.3%。最终出水的化学需氧量仅为85毫克/升,五日生化需氧量为10毫克/升。在pH值为7 - 8、添加300毫克/升过氧化氢且反应持续30分钟的条件下,臭氧氧化最为有效。臭氧氧化还显著提高了有机残余物的生物降解性。这些残余物中近50%可作为反硝化的碳源。