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机构地区:[1]清华大学环境工程系
出 处:《环境科学》1995年第3期8-11,54,共5页Environmental Science
基 金:国家自然科学基金
摘 要:采用硫酸盐还原-生物脱除硫化物-甲烷化的方法,考察了酸相反应器的运行效果,以及系统的操作条件和运行情况等。结果表明:①以拉西瓷环为填料的厌氧滤地作为酸相反应器,容积负荷可达5kg/(m3·d),去除率为80%;②在脱硫化物反应器中,硫化物去除率大于90%,其中95%的硫化物转化为S0;③甲烷相反应器COD容积负荷可达15.8kg/(m3·d),COD去除率为83.3%。整体工艺COD去除率为87.6%,去除率为99.4%-100%。two-phase anaerobic digestion process has been developed for treating high strength organic wastewater containing a high level Of Sulphate.The system comprises: ac anaerobic filter packed with Rasching rings which was used as an acidogenie reactor wilh a volumetric loading of 5 kg SO-/(m3. d) and a SO- removal efficiency of 80% ;② a desulphiding reactor with a sulphide removal rate of more than 90%, of which more than 95% was converted to S0;③ a methanogenic reactor with a COD volumetric loading rate Of 15. 8 kg COD/(m3. d) and a COD removal efficiency of 83. 3%. The whole system has an overall COD removal efficiency of 87. 6% and a SO removal efficiency of 99. 4%-100%.
分 类 号:X703[环境科学与工程—环境工程]
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