安徽农学通报
安徽農學通報
안휘농학통보
AUHUI AGRICULTURAL SCIENCE BULLETIN
2014年
13期
25-28
,共4页
唐中亚%邓飞飞%孔为丽%岳梅
唐中亞%鄧飛飛%孔為麗%嶽梅
당중아%산비비%공위려%악매
渗滤液%A/O工艺%菌种驯化%碳氮比
滲濾液%A/O工藝%菌種馴化%碳氮比
삼려액%A/O공예%균충순화%탄담비
Leachate%A/O process%Domestication of bacteria%Ratio of carbon and nitrogen
对高浓度渗滤液进行生化处理具有局限性,尤其对在初期无法完全降解渗滤液中难降解的特殊有机物质,需对菌种污泥进行驯化。该研究基于实际工程案例,总结2个月渗滤液生化处理技术工程中初始调试期的污泥培养技术及其影响因素参数控制。菌种污泥含水量80%左右,采用低负荷培养驯化的模式,按照先好氧后厌氧培养的顺序,驯化初期的原水稀释倍数为10倍,生化内回流比为3,控制生化池碳氮比为5∶1,在污泥培养驯化期间注意调控硝化及反硝化池中的pH、温度、碱度、溶解氧等环境影响参数。经过调试后,生化处理系统出水水质为NH3-N 12~27mg/L、CODcr 58~107mg/L、pH 6.8~8.0,出水水质满足后续MRB工艺要求[1]。
對高濃度滲濾液進行生化處理具有跼限性,尤其對在初期無法完全降解滲濾液中難降解的特殊有機物質,需對菌種汙泥進行馴化。該研究基于實際工程案例,總結2箇月滲濾液生化處理技術工程中初始調試期的汙泥培養技術及其影響因素參數控製。菌種汙泥含水量80%左右,採用低負荷培養馴化的模式,按照先好氧後厭氧培養的順序,馴化初期的原水稀釋倍數為10倍,生化內迴流比為3,控製生化池碳氮比為5∶1,在汙泥培養馴化期間註意調控硝化及反硝化池中的pH、溫度、堿度、溶解氧等環境影響參數。經過調試後,生化處理繫統齣水水質為NH3-N 12~27mg/L、CODcr 58~107mg/L、pH 6.8~8.0,齣水水質滿足後續MRB工藝要求[1]。
대고농도삼려액진행생화처리구유국한성,우기대재초기무법완전강해삼려액중난강해적특수유궤물질,수대균충오니진행순화。해연구기우실제공정안례,총결2개월삼려액생화처리기술공정중초시조시기적오니배양기술급기영향인소삼수공제。균충오니함수량80%좌우,채용저부하배양순화적모식,안조선호양후염양배양적순서,순화초기적원수희석배수위10배,생화내회류비위3,공제생화지탄담비위5∶1,재오니배양순화기간주의조공초화급반초화지중적pH、온도、감도、용해양등배경영향삼수。경과조시후,생화처리계통출수수질위NH3-N 12~27mg/L、CODcr 58~107mg/L、pH 6.8~8.0,출수수질만족후속MRB공예요구[1]。
There are limitations in the biochemical treatment of high concentrations leachate. Especially when the biodegradable organic objects in the leachate can not be completely degraded in beginning,So the sludge of bacteria need to be acclimated. The study is based on actual project case. Sludge cultivation techniques and relevant factors in biochemical treatment technology of landfill leachate projects during two months’ debugging step are summed up. The using Sludge which have about 80% water,and choose the low load domestication and cultivation mode.The sludge is cultivated through aerobic digestion before anaer-obic digestion. raw water dilution ratio is controled to 10 times, Internal biochemical reflux reflux ratio is 3,with carbon nitrogen ratio of 5:1,During the cultivating process,denitrification and pH,temperature,al-kalinity, dissolved oxygen and other influencing parameters should be regulated. After debugging, effluent water quality can reach the requirements of subsequent MBR process with NH3-N content of 12~27mg/L, CODcr,58~107mg/L,pH6.8~8.0.