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Student Number 89326020
Author Mei-Chu Kuang(康美祝)
Author's Email Address No Public.
Statistics This thesis had been viewed 3152 times. Download 2314 times.
Department Graduate Institute of Environmental Engineering
Year 2001
Semester 2
Degree Master
Type of Document Master's Thesis
Language zh-TW.Big5 Chinese
Title The characteristic of MBR system in removal nitrogen
Date of Defense 2002-05-31
Page Count 93
Keyword
  • aerobic denitrifier
  • HRT
  • MBR
  • reflux ratio
  • SRT
  • Abstract The Membrane bioreactor (MBR) is the combination of the activated sludge process and the membrane technique process. With the effective filtrating function of the membrane unit, the suspended solid (SS) in the effluent of an MBR can be reduced to a very low concentration, hence eliminating the requirement of a secondary clarifier. This combination could further simplify the complicated operation requirements of the traditional wastewater secondary treatment facilities and is beneficial to the economic aspects of a treatment process for its less land demand.
    In this study, we first surveyed the impact of different hydraulic retention time (HRT) on an MBR. With a fixed sludge retention time (SRT=10 days), pH value (6.8~7.1), dissolved oxygen concentration (DO=5mg/L) and varied HRT (5, 10, 15, 20 hours), the MBR removed influent ammonia-nitrogen (NH4+-N) and chemical oxygen demand (COD) with high efficiency (100% and 94% respectively), and the best treatment efficiency was obtained with an HRT equaled to15 hours. However, the MBR didn’t display a function of phosphorus removal.
    To further increase the nitrogen removing efficiency of the MBR system, an anoxic tank was added in the upper stream of the aerobic MBR, which formed a two-stage MBR. With varied reflux ratio of the aerobic tank effluent to the influent (0.5, 1.5 and 2.0 respectively), the two-stage MBR removed COD and NH4+-N significantly, but the removal of phosphorus was not largely increased (efficiency =25%). The best COD and NH4+-N removing efficiency was obtained with the reflux ratio of 1.5.
    Utilizing the optimized HRT and reflux ratio, we further tested the two-stage MBR system with different sludge retention time (SRT=10, 20 and 30 days). Results showed that the two-stage MBR performed stably and the total nitrogen removal efficiency could reach 81% with a SRT of 30 days. Moreover, 16S rDNA analysis of the system showed that bacteria belonged to Proteobacteria and Planctomycetale groups existed in the microbial community of the two-stage MBR reactor. We also found aerobic denitrifier at varied SRT.
    Table of Content 目錄……………………………………………………………………Ⅰ
    圖目錄…………………………………………………………………Ⅳ
    表目錄…………………………………………………………………Ⅷ
    第一章 前言…………………………………………………………1
    1.1 研究動機……………………………………………...................1
    1.2 研究目的……………………………………………...................2
    第二章 文獻回顧……………………………………………………3
    2.1 生物處理法……………………………..………………………..3
    2.1.1 生物處理法原理………………..………………………….3
    2.1.2 生物硝化、脫硝原理………………………………………4
    2.1.3 生物除磷原理………………………………………...........9
    2.1.4 生物處理法種類概述………………………………...........11
    2.1.5 生物處理程序中常見之微生物……………………...........15
    2.2 薄膜生物程序……………………………………………............15
    2.2.1 薄膜種類……………………………………………...........16
    2.2.2 MBR種類………………………………………………….18
    2.2.3 固液分離MBR形式………………………………………19
    2.2.4 MBR與CAS之比較………………………………...........21
    2.3 沈浸式好氧MBR程序處理都市污水之利用………………….24
    2.3.1 有機負荷與水力停留時間…………………………...........26
    2.3.2 氮、磷之去除……………………………………………….26
    2.3.3 微生物………………………………………………...........27
    2.3.4 薄膜孔徑與通量……………………………………...........27
    2.4 利用分子生物技術探討微生物菌群結構………………………28
    2.4.1 分子生物學…………………………………………...........28
    2.4.2 總DNA之萃取……………………………………………30
    2.4.3 聚合酵素連鎖反應…………………………………...........31
    2.4.4 分子轉殖…………………………………...........................31
    2.4.5 變性梯度明膠電泳…………………………………...........32
    第三章 實驗設備與方法……………………………………………..33
    3.1 實驗設備與實驗計畫…………………………….……………...33
    3.1.1 實驗設備……………………….…………………………..33
    3.1.2 模型廠實驗計畫……………….…………………………..36
    3.2 實驗步驟…………………………………….……………...........37
    3.3 分析方法與設備…………………………………………………38
    3.3.1 水質分析方法………………………………………...........38
    3.3.2 菌相分析方法………………………………………...........38
    3.3.3 分析設備……………………………………………...........43
    第四章 結果與討論…………………………………………………..44
    4.1 控制不同HRT下MBR程序之處理特性………….…………..45
    4.1.1 單槽MBR程序對於碳、氮、磷之處理效果……………..45
    4.1.2 單槽MBR處理結果比較………………………………….49
    4.1.3 單槽MBR程序於HRT=20hr之菌相分析……………….53
    4.2 兩段式MBR程序不同硝化液迴流比之處理特性….………….54
    4.2.1 MBR程序對於碳、氮、磷之處理效果………………….55
    4.2.2 MBR程序於不同硝化液迴流比處理結果比較…………..57
    4.3 兩段式MBR程序控制不同SRT下之處理特性……………….60
    4.3.1 MBR程序對於碳、氮、磷之處理效果…………………..60
    4.3.2 MBR程序於不同SRT時各處理單元之水質分析……….62
    4.4 MBR程序於不同SRT時之菌相分析…………………………….66
    4.4.1 MBR程序在SRT=10天之菌相分析……………………..66
    4.4.2 MBR程序在SRT=20天之菌相分析…………………….72
    4.4.3 MBR程序在SRT=30天之菌相分析…………………….78
    4.4.4 MBR程序在不同SRT之菌相綜合比較………………….83
    第五章 結論與建議…………………………………………………..86
    5.1結論…………………………………………………………...........86
    5.2 建議………………………………………………………………..87
    參考文獻………………………………………………………………89
    圖 目 錄
    圖2.1 傳統活性污泥法3
    圖2.2 氮處理程序中氮的轉換4
    圖2.3 磷蓄積菌厭氧/好氧代謝模式示意圖10
    圖2.4 厭氧/缺氧/好氧程序對於磷及氮去除模式示意圖10
    圖2.5 WUHRMAN除氮程序11
    圖2.6 MLE除氮程序12
    圖2.7 BARDENPHO除氮程序12
    圖2.8 相分離氧化渠脫氮處理程序13
    圖2.9 多段式旋轉圓盤處理設施斷面圖13
    圖2.10 PEGASUS除氮程序14
    圖2.11 生物膜之淨化圖(修正WILLIAM, 1989)15
    圖2.12 濾膜孔徑與污染物粒俓關係圖18
    圖2.13 (A)固液分離薄膜程序;(B)氧傳輸薄膜程序(MABR);(C)萃取薄膜程序(EMBR)19
    圖2.14 MBR程序之配置方式20
    圖2.15 薄膜生物程序圖21
    圖2.16 分子生物技術在環境微生物多樣性分析流程30
    圖3.1 MBR模廠示意圖35
    圖3.2 實驗流程圖37
    圖3.3 分子生物實驗流程圖39
    圖4.1 單槽MBR程序對於碳、氮、磷之去除效率48
    圖4.2 單槽MBR程序於不同HRT時好氧槽之MLSS及MLVSS48
    圖4.3 單槽MBR程序於不同HRT之出流水總菌落數49
    圖4.4 單槽MBR程序於各處理程序之COD濃度50
    圖4.5 單槽MBR程序於各處理程序之氨氮濃度51
    圖4.6 單槽MBR程序於各處理程序之TKN濃度51
    圖4.7 單槽MBR程序於各處理程序之總氮濃度52
    圖4.8 單槽MBR程序於各處理程序之總磷濃度52
    圖4.9 各處理階段COD之濃度變化58
    圖4.10 各處理階段TP之濃度變化58
    圖4.11 各處理階段氨氮之濃度變化59
    圖4.12 各處理階段NOX之濃度變化59
    圖4.13 不同SRT各處理階段COD之濃度變化63
    圖4.14 不同SRT各處理階段氨氮之濃度變化63
    圖4.15 不同SRT各處理階段TKN之濃度變化64
    圖4.16 不同SRT各處理階段NOX之濃度變化64
    圖4.17 不同SRT各處理階段TN之濃度變化65
    圖4.18 不同SRT各處理階段TP之濃度變化65
    圖4.19 SRT=10天之DGGE菌相分布圖67
    圖4.20 MBR程序在SRT=10天之菌相分布圖68
    圖4.21 以16RDNA為基礎對SRT=10天之污泥樣品製作之親緣樹69
    圖4.22 SRT=20天之DGGE菌相分布圖73
    圖4.23 MBR程序在SRT=20天之菌相分布圖74
    圖4.24 以16RDNA為基礎對SRT=20天之污泥樣品製作之親緣樹75
    圖4.25 SRT=30天之DGGE菌相分布圖79
    圖4.26 MBR程序在SRT=30天之菌相分布圖79
    圖4.27 MBR程序在SRT=30天之菌相分布圖................................81
    圖4.28 各試程之菌種分布圖84
    表目錄
    表2.1 生物處理脫氮作用機制……………………………………..7
    表2.2 生物處理除磷之步驟………………………………………..10
    表2.3 生物營養鹽處理程序中常見的微生物菌屬………………..16
    表2.4 MBR與CAS處理廢水結果之比較…………………………22
    表2.5 MBR與CAS於不同SRT之Yield…………………………..22
    表.2.6 好氧MBR程序在處理都市廢水時的水力停留時間及有機負荷之特性…………………………………………………..
    25
    表2.7 沈浸式MBR程序常用之孔徑及通量……………………….28
    表3.1 人工合成污水之主要水質…………………………………..34
    表3.2 人工合成污水之主要水質…………………………………..34
    表3.3 MBR模廠各實驗室成之控制條件…………………………36
    表3.4 聚合酵素連鎖反應之引子…………………………………..41
    表4.1 各實驗試程之控制條件及討論章節………………………..44
    表4.2 進流水質負荷及操作條件…………………………………..46
    表4.3 單一好氧槽MBR程序於不同HRT時之處理效果……….46
    表4.4 單槽MBR程序於HRT=20小時之優勢菌種……………..53
    表4.5 MBR程序於不同硝化液迴流比時之處理效果…………….56
    表4.6 MBR於不同SRT時之處理效果……………………………..........61
    表4.7 SRT=10之親緣樹內各菌株分類…………………………..70
    表4.8 SRT=20之親緣樹內各菌株分類…………………………..76
    表4.9 SRT=30之親緣樹內各菌株分類…………………………..82
    表4.10 各試程具有除氮弁鄐孝葴堣嬪G………………………….85
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    Date of Submission 2002-06-10

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