中国环境科学
中國環境科學
중국배경과학
CHINA ENVIRONMENTAL SCIENCE
2014年
7期
1728-1733
,共6页
郑冰玉%张树军%张亮%杨岸明%彭永臻
鄭冰玉%張樹軍%張亮%楊岸明%彭永臻
정빙옥%장수군%장량%양안명%팽영진
垃圾渗滤液%厌氧氨氧化%除碳%脱氮
垃圾滲濾液%厭氧氨氧化%除碳%脫氮
랄급삼려액%염양안양화%제탄%탈담
landfill leachate%anaerobic ammonia oxidation%decarbonize%nitrogen removal
以垃圾渗滤液为研究对象,研究UASB-除碳-一体化ANAMMOX工艺的除碳脱氮特性.结果表明:该工艺可实现高效除碳脱氮;在进水COD浓度6210~16365mg/L?TN浓度为990~2100mg/L时工艺出水COD浓度最低为655mg/L,出水TN浓度最低为39.9mg/L.进水中的可降解COD主要在UASB和除碳池中去除(分别为59%和31%),进入到一体化ANAMMOX池中的多为惰性有机物质;TN的去除在除碳池和一体化ANAMMOX池中进行,其中除碳池中TN去除量占工艺TN去除量的53%,主要通过同步硝化反硝化去除;ANAMMOX池中TN去除46%,主要通过AOB和AnAOB的协同作用实现.当除碳池出水含可降解有机物时,对后续一体化ANAMMOX池的自养脱氮抑制严重;充分降解除碳池中的可降解有机物是影响系统脱氮效率的关键因素.
以垃圾滲濾液為研究對象,研究UASB-除碳-一體化ANAMMOX工藝的除碳脫氮特性.結果錶明:該工藝可實現高效除碳脫氮;在進水COD濃度6210~16365mg/L?TN濃度為990~2100mg/L時工藝齣水COD濃度最低為655mg/L,齣水TN濃度最低為39.9mg/L.進水中的可降解COD主要在UASB和除碳池中去除(分彆為59%和31%),進入到一體化ANAMMOX池中的多為惰性有機物質;TN的去除在除碳池和一體化ANAMMOX池中進行,其中除碳池中TN去除量佔工藝TN去除量的53%,主要通過同步硝化反硝化去除;ANAMMOX池中TN去除46%,主要通過AOB和AnAOB的協同作用實現.噹除碳池齣水含可降解有機物時,對後續一體化ANAMMOX池的自養脫氮抑製嚴重;充分降解除碳池中的可降解有機物是影響繫統脫氮效率的關鍵因素.
이랄급삼려액위연구대상,연구UASB-제탄-일체화ANAMMOX공예적제탄탈담특성.결과표명:해공예가실현고효제탄탈담;재진수COD농도6210~16365mg/L?TN농도위990~2100mg/L시공예출수COD농도최저위655mg/L,출수TN농도최저위39.9mg/L.진수중적가강해COD주요재UASB화제탄지중거제(분별위59%화31%),진입도일체화ANAMMOX지중적다위타성유궤물질;TN적거제재제탄지화일체화ANAMMOX지중진행,기중제탄지중TN거제량점공예TN거제량적53%,주요통과동보초화반초화거제;ANAMMOX지중TN거제46%,주요통과AOB화AnAOB적협동작용실현.당제탄지출수함가강해유궤물시,대후속일체화ANAMMOX지적자양탈담억제엄중;충분강해제탄지중적가강해유궤물시영향계통탈담효솔적관건인소.
Landfill leachate as the research object, the organics and nitrogen removal characteristics of UASB- decarbonize-integrated ANAMMOX process were studied. The results showed that: the process can achieve efficient carbon removal. With the influent COD concentration of 6210-16365mg/L, TN concentration of 990-2100mg/L, the effluent COD concentration was 655mg/L, the minimum effluent TN concentration was 39.9mg/L. Influent biodegradable COD were mainly removed in UASB and decarbonize tank. The removal efficiency was respectively 59% and 31%. while the left inert organic substances flowed into the integration ANAMMOX tank. TN removal took place in decarbonizes and integrated ANAMMOX tank. TN removal in decarbonize tank accounted for 53%, which was mainly through denitrification and simultaneous nitrification and denitrification removal. TN removal in ANAMMOX tank accounted for 46%, which was mainly through the synergy of AOB and AnAOB. When the effluent of decarbonize tank contained biodegradable organic matters, the autotrophic nitrogen removal process in the subsequent integration ANAMMOX tank was inhibited seriously. Full degradation of organics in decarbonize tank is the key factor for effective nitrogen removal in the whole system.