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研究生:藍英韡
研究生(外文):Lan, Ying-Wei
論文名稱:懸浮與附著生長對基質的競爭作用
論文名稱(外文):Substrate Competition between Suspended and Attached Growths
指導教授:李志源李志源引用關係
指導教授(外文):Lee, Chi-Yuan
學位類別:碩士
校院名稱:國立屏東科技大學
系所名稱:環境工程技術研究所
學門:工程學門
學類:環境工程學類
論文種類:學術論文
論文出版年:1995
畢業學年度:83
語文別:中文
論文頁數:114
中文關鍵詞:混合式反應器模式動力參數穩定狀態生物旋轉盤
外文關鍵詞:hybrid reactormodelkinetic coefficientssteadt staterotating biological contactors
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  本研究之目的是以實驗室規模之反應器探討懸浮與附著兩生長
系對基質之競爭使用現象,所得數據同時將驗證Lee(1992)所導模
式之正確性。研究工作主要分為兩部分進行。第一部分為模式動力
參數之檢定。第二部分為連續運轉混生反應器,以瞭解競爭行為並
進行模式的驗證工作。
  參數檢定試驗中,首先利用化學恆定器求取Monod動力參數,
其值分別為k=4.13mg TOC/mg VSS-day、Ks=10.77mg TOC/L、
Y=0.79mg VSS/mg TOC與bd=0.19day-1。實驗同時發現生物膜細菌
密度(Xf)在15-25g/L間。在生物膜剝落係數(bs)之測定中,當生物
旋轉盤的轉速在5rpm、10rpm與15rpm時,剝落率並無很大的差異;
當轉速定在10rpm,剝落率與Xf、Lf(Lf為生物膜厚度)乘積有關,
對應之bs為0.22day-1。上述實驗所得之模式參數,經進行敏感度
分析後,我們發現k、Y、bs最為重要。k與Y值的增加有利懸浮性生
長之競爭使用基質,此結果可降低放流水基質濃度。另外,增加bs
值,雖亦能增加懸浮微生量(Xe),但因此生長系之微生物容易被洗
出,故會增加放流水基質濃度。
  連續運轉混生反應器所得結果指出,兩生長系對基質之競爭使
用與進流水基質濃度及操作停留時間有關。進流水基質濃度愈高愈
有助提昇懸浮生長系比例。長的水力停留時間會提昇附著生長,但
長的固體停留時間發現並沒有增強懸浮生長,此與模式所預測現象
並不相符,其原因尚待探討。
  在不同之操作條件下,將試驗所得值迴歸分析後與模式預測值
比對,發現有若干差異,例如:就放流水基質濃度言,模式之最佳
預測範圍約在Se=4mg TOC/L附近。此外,模式所預測之懸浮生物量
及懸浮生長系比率均有偏高現象。至於生物膜厚度模式預測值則低
於試驗值。雖然如此,整體而言,該模式仍成功地預測出不同操作
狀況下,兩生長系之競爭結果,尤具在低負荷,懸浮生長系不顯著
的環境,模式預測值與實驗值相當接近。


This research is intended to unravel the mystery of substrate competition between suspended and attached microorganisms in a completely mixed reactor, called hybrid reactor. Results obtained from this study was also used for evaluating a model (Lee, 1992) developed for describing the competition behaviors. There were two experimental phases conducted in this research: estimation of the corresponding kinetic coefficients and evaluation of performance f a laboratory-scale hybrid reactor.
Based on Chemostat technique, the estimation of standard Monod coefficients of k, Ks, Y, and bd were found as 4.13 mg TOC/mg VSS-day, 10.68 mg TOC/L, 0.79 mg VSS/mg TOC, and 0.19 day-1, respectively. The biofilm detachment rate perofrmed with a biofilm reactor (submerged rotating biological contactors) appeared independent to the disc speed as controlled at 5, 10, and 15 rpm. However, it was related to the product of Xf (biofilm density) and Lf (biofilm thickness); best fit of the detachment coefficient was 0.216 day-1. In additiion, experimental results also showed that the value of Xf varied in the range of 15-25 g/L. Sensitivity analyses of the above parameters revealed that k, Y, and bs are the most important. Higher values of k and Y encourage suspended growth to compete for substrate which yields better effluent quality; while the increase of bs would promote suspended growth through which effluent quality is deteriorated.
Results of continuous operation of the hybrid reactor indicated that the substrate competition by the two growths depended on substrate loads (So), hydraulic detention time (HRT), and solids retention time (SRT). Both effects of heavy loads of So and longer HRT brought about the suspended growth more competitive; while SRT did not play important role in affecting the competing behaviors. When the data obtained from the experiments were compared with the model predictions, a little discrepancy was found, such as that the predicted effluent levels agree with the measured values only occurring around 4 mg TOC/L. Furthermore, the amount of suspended biomass as well as the fraction of suspended growth are overestimated which result in a lower predicted competition of attached grwoth. Nevertheless, in general the model successfully predicts the competing results at the operating conditions. Especially, when the suspended growth is not predominant the predictions are very close to the measured values.

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