环境工程学报
環境工程學報
배경공정학보
CHINESE JOURNAL OF ENVIRONMENTAL ENGINEERING
2010年
2期
278-282
,共5页
冯宗强%袁旭峰%林长松%王晓芬%崔宗均%李虎林
馮宗彊%袁旭峰%林長鬆%王曉芬%崔宗均%李虎林
풍종강%원욱봉%림장송%왕효분%최종균%리호림
固定床厌氧反应器%猪粪尿%厌氧处理
固定床厭氧反應器%豬糞尿%厭氧處理
고정상염양반응기%저분뇨%염양처리
anaerobic pecked bed reactor%pig waste%anaerobic treatment
为开展高效厌氧生物技术处理家禽粪便的应用研究,试验依据固定床厌氧反应器(anaerobic pecked bed reac-tor)的特点,设计了一个有效容积为20 L的高效厌氧反应器,以猪粪尿为发酵原料,进水COD浓度范围在4 820~54 000mg/L,实验过程为55 d.按进料的水力停留时间可将实验划分为2个阶段:前期(44 d)和后期(11 d),前期通过提高进料浓度直接提高反应器处理浓度,水力停留时间保持为2 d,每7~8 d为一个周期;后期通过缩短水力停留时间间接提高反应器处理浓度,进料浓度保持不变,每2~3 d为一个周期.通过对厌氧处理系统运行过程中 COD、pH、挥发性成分、TN、TP和NH_3-N含黾的测定,分析了该系统运行特点.结果表明:在发酵的第1~55 d,整个厌氧处理系统能够稳定运行,COD去除率稳定在67%~88%之间;对TN、TP、NH_3-N都有很好的去除能力.
為開展高效厭氧生物技術處理傢禽糞便的應用研究,試驗依據固定床厭氧反應器(anaerobic pecked bed reac-tor)的特點,設計瞭一箇有效容積為20 L的高效厭氧反應器,以豬糞尿為髮酵原料,進水COD濃度範圍在4 820~54 000mg/L,實驗過程為55 d.按進料的水力停留時間可將實驗劃分為2箇階段:前期(44 d)和後期(11 d),前期通過提高進料濃度直接提高反應器處理濃度,水力停留時間保持為2 d,每7~8 d為一箇週期;後期通過縮短水力停留時間間接提高反應器處理濃度,進料濃度保持不變,每2~3 d為一箇週期.通過對厭氧處理繫統運行過程中 COD、pH、揮髮性成分、TN、TP和NH_3-N含黽的測定,分析瞭該繫統運行特點.結果錶明:在髮酵的第1~55 d,整箇厭氧處理繫統能夠穩定運行,COD去除率穩定在67%~88%之間;對TN、TP、NH_3-N都有很好的去除能力.
위개전고효염양생물기술처리가금분편적응용연구,시험의거고정상염양반응기(anaerobic pecked bed reac-tor)적특점,설계료일개유효용적위20 L적고효염양반응기,이저분뇨위발효원료,진수COD농도범위재4 820~54 000mg/L,실험과정위55 d.안진료적수력정류시간가장실험화분위2개계단:전기(44 d)화후기(11 d),전기통과제고진료농도직접제고반응기처리농도,수력정류시간보지위2 d,매7~8 d위일개주기;후기통과축단수력정류시간간접제고반응기처리농도,진료농도보지불변,매2~3 d위일개주기.통과대염양처리계통운행과정중 COD、pH、휘발성성분、TN、TP화NH_3-N함민적측정,분석료해계통운행특점.결과표명:재발효적제1~55 d,정개염양처리계통능구은정운행,COD거제솔은정재67%~88%지간;대TN、TP、NH_3-N도유흔호적거제능력.
In order to research on a highly-effective disposal of poultry manure through anaerobic biotech-nology, an efficient anaerobic reactor with an effective volume of 20 L was designed according to the characteris-tics of anaerobic pecked bed reactor. Pen manure as raw material for fermentation, the raw water COD was adjus-ted between 4 820 and 54 000 mg/L. The whole process was 55 days, which was divided into two stages accord-ing to the raw of hydraulic retention time: the prophase (44 d) and the anaphase (11 d) ,in the prophase the dealing concentration of reactor was directly advanced by increasing the raw water concentration, the hydraulic remain time ( HRT) was maintained 2 days, 7 ~8 days per cycle. In the anaphase, the dealing concentration of reactor was indirectly advanced by shortening the residence time, and the influent concentration was unchanged, 2~3 days per cycle. COD, pH, volatile components and the content of TN,TP and NH_3-N were determined through to the whole procession in the anaerobic treatment system, and analysis of operating characteristics of the system. Results demonstrated that in the fermentation section 1~55 d, the whole system could be stably opera-ted, with a stable COD removal efficiency which were between 67% and 88% ; and high capacity in removing TN ,TP and NH_3-N.