广东化工
廣東化工
엄동화공
GUANGDONG CHEMICAL INDUSTRY
2012年
7期
26-28
,共3页
连续流%好氧颗粒污泥%同步脱氮除磷
連續流%好氧顆粒汙泥%同步脫氮除燐
련속류%호양과립오니%동보탈담제린
continuous flow: aerobic granular sludge: simultaneous nitrogen and phosphorus removal
在上流式污泥床好氧颗粒污泥反应器中，以厌氧颗粒污泥为接种泥．采用人工配制的模拟废水为进水的条件下，成功培养出具有同步脱氮除磷的好氧颗粒污泥。颗粒污泥粒径在0．5~2mm，颗粒污泥沉淀速度在29～58m／h。MLSS为3077---4103mg／L。当COD的进水容积负荷为4．8kg／（m3·d）时，去除率高达96％以上。氨氮进水在160mg／L时，去除率达97％以上，出水氨氮在5mg／L以下。对总磷的去除率在22％-37％。主要是因为亚硝态氮浓度、COD／TN比和TN／TP比等对聚磷菌除磷有影响。
在上流式汙泥床好氧顆粒汙泥反應器中，以厭氧顆粒汙泥為接種泥．採用人工配製的模擬廢水為進水的條件下，成功培養齣具有同步脫氮除燐的好氧顆粒汙泥。顆粒汙泥粒徑在0．5~2mm，顆粒汙泥沉澱速度在29～58m／h。MLSS為3077---4103mg／L。噹COD的進水容積負荷為4．8kg／（m3·d）時，去除率高達96％以上。氨氮進水在160mg／L時，去除率達97％以上，齣水氨氮在5mg／L以下。對總燐的去除率在22％-37％。主要是因為亞硝態氮濃度、COD／TN比和TN／TP比等對聚燐菌除燐有影響。
재상류식오니상호양과립오니반응기중，이염양과립오니위접충니．채용인공배제적모의폐수위진수적조건하，성공배양출구유동보탈담제린적호양과립오니。과립오니립경재0．5~2mm，과립오니침정속도재29～58m／h。MLSS위3077---4103mg／L。당COD적진수용적부하위4．8kg／（m3·d）시，거제솔고체96％이상。안담진수재160mg／L시，거제솔체97％이상，출수안담재5mg／L이하。대총린적거제솔재22％-37％。주요시인위아초태담농도、COD／TN비화TN／TP비등대취린균제린유영향。
The successful cultivation of aerobic granular sludge used for simultaneous nitrogen and phosphorus removal in airlift aerobic granular sludge bed reactor（AGSB） which was inoculated anaerobic granular sludge and was performed using a synthetic wastewater mainly consisted of glucose as carbon source. The diameters of the granules were 0.5-2 mm, the settling velocity were 29-58 m/h, MLSS of 3077--4103 mg/L. As the COD loading of 4.8 kg/（m3.d）were employed, COD removal efficiency of above 96 %. When the ammonia nitrogen concentration of 160 mg/L was used as the influent to the reactor, the removal rate of ammonia nitrogen was 97 % and the ammonia nitrogen concentration of effluent was low as 5 mg/L The remove rate of TP was 22 %-37 %. The main reason was that the concentration of nitrite and the radios ofCOD/TN, TN/TP impact the TP removal efficiency.
