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研究生: 柯銀府
Yin-Fu Ko
論文名稱: 蘇力菌醱酵系統之動態分析
Dynamic Analysis of the Fermentation of Bacillus thuringiensis
指導教授: 吳文騰
Wen-Teng Wu
口試委員:
學位類別: 碩士
Master
系所名稱: 工學院 - 化學工程學系
Department of Chemical Engineering
論文出版年: 2000
畢業學年度: 88
語文別: 中文
論文頁數: 88
中文關鍵詞: 蘇力菌蘇力菌素動態脈衝
外文關鍵詞: Bacillus thuringiensis, thuringiensin, dynamic, pulse
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  • 摘要
    生物農藥已然成為國家未來優先發展之生技產業之一,而最廣為農用的便是蘇力菌製劑。本研究使用的菌株,蘇力菌達姆斯塔丁斯亞種(Bacillus thuringiensis subsp. darmstadiensis, HD-199)所生產之蘇力菌素,因具熱穩定性和廣譜殺蟲作用,適可彌補δ-內毒素之不足,增加殺蟲能力,故有商業化潛力。產品要商業化,便要透過規模放大的技術,而規模放大之前充分地瞭解系統,有助於成功的放大。

    本研究在於利用小規模醱酵槽來探討放大規模時所必需注意的混合問題。在混合良好的實驗室規模醱酵槽,運用pH block pulse及pH periodic variation的技巧來營造混合不佳時的擾動情形,以研究在大規模醱酵槽中,若混合不佳且由於控制pH值時添加酸鹼所造成的影響。結果發現,在生長停滯期,酸鹼值的擾動對系統不會造成影響,但在對數生長期中的擾動則同時影響到菌體生長及產物的生成,且對菌體影響甚於產物。另外,本研究同時運用攪拌速率及通氣量的block pulse及step change 之技巧以探討氧氣質傳以及剪應力在不同時期所造成的影響。結果發現,在對數生長期時氧氣質傳扮演重要角色,供氧不足造成菌體生長受限,產物也隨之降低;在生長停滯期降低剪應力有助於產物的生成。


    Abstract
    Bioinsecticide is one of the important products of bioindustries. In Taiwan, the government is promoting. The bioinsecticides derived from Bacillus thuringiensis have been globally used. Thuringiensin which is heat-stable with broadly insecticidal activity is produced by Bacillus thuringiensis subsp. darmstadiensis, HD-199, in this study. Thuringiensin can improve the insecticidal activity of the traditional biocontrol agent derived fromδ-endotoxin. So it have highly commercial potential. Scale-up of the fermentor makes the commercialization come true. Understanding the dynamics of the fermentation system can contribute a satisfactory scale-up.

    In this study, mixing, which is an important factor in large-scale fermentor, is investigated in the laboratory scale fermentor. In the laboratory scale fermentor, which is well mixed, the technique of pH block pulse and pH periodic variation is employed. The change of pH value simulates poor mixing in a large-scale fermentor. We found that the variations of pH did not have effects on the production of product during the stationary phase, but significantly affected both the growth of microbes and the production of thuringiensin during the exponential phase.

    Similarly, we introduced the block pulse and step change of agitation and aeration to investigate the problem of oxygen transfer and the effect of shear stress. The oxygen transfer played an important role during the exponential phase. It limited the growth of the microbes and reduced the production of thuringiensin, if the oxygen was not sufficiently provided. The yield could be improved by reducing the agitation rate during the stationary phase.

    目錄 摘要 英文摘要(Abstract) 謝誌 目錄 表目錄 圖目錄 第一章 緒論 1-1 前言 1-2 生物性農藥 1-2-1 生物殺蟲劑-蘇力菌製劑 1-2-2 蘇力菌素 1-3 醱酵系統之動態行為 1-3-1 醱酵系統的動態研究 1-3-2 研究動機 1-4 章節組織 第二章 實驗材料與方法 2-1 實驗材料 2-1-1 菌株(strain) 2-1-2 培養基(medium) 2-2 實驗方法及條件 2-2-1 前培養 2-2-2 主培養(批次醱酵培養) 2-3 實驗設備與配置 2-4 分析方法 2-4-1 菌體數之測定 2-4-2 還原糖濃度之分析 2-4-3 蘇力菌素之分析法 第三章 結果與討論 3-1 酸鹼值(pH)對醱酵系統的影響 3-1-1 不同酸鹼值之培養 3-1-2 pH值的擾動測試 3-1-2-1 pH值的脈衝擾動測試 3-1-2-2 pH值的step change測試 3-1-2-3 不同生長期之pH擾動影響 3-2 氧氣質傳(kLa)及剪應力(shear stress)的影響 3-2-1 對數生長期之block pulse 測試 3-2-2 生長停滯期之step change 測試 第四章 結論與未來展望 4-1 結論 4-1-1 酸鹼(pH)值擾動 4-1-2 氧氣質傳(kLa)及剪應力的影響 4-2 未來展望 參考文獻1 表目錄 表2-1 蘇力菌培養及保存用之固態平面培養基之組成 表2-2 蘇力菌前培養之液態培養基組成 表2-3 蘇力菌醱酵主培養基組成 表2-4 蘇力菌培養之醱酵條件 表2-5 醱酵系統周邊設備、線上及非線上分析儀器規格 表2-5 (續)醱酵系統之周邊設備、線上及非線上分析儀器規格 表3-1 run-1實驗組之結果 表3-2 run-2實驗組之結果 表3-3 run-3實驗組之結果 表3-4 run-4實驗組之結果 表3-5 run-5實驗組之結果 表3-6 不同實驗組之氧氣質傳係數(kLa)比值 表3-7 不同攪拌速率下的尖端速度 圖目錄 圖1-1 蘇力菌素之化學結構式 圖2-1 批式醱酵系統設備裝置圖 圖3-1 run-1A之蘇力菌醱酵系統走勢圖 圖3-2 run-1B之蘇力菌醱酵系統走勢圖 圖3-3 run-1實驗組之比較圖 圖3-4 run-2A之蘇力菌醱酵系統走勢圖 圖3-5 run-2B 之蘇力菌醱酵系統走勢圖 圖3-6 run-2C 之蘇力菌醱酵系統走勢圖 圖3-7 run-2A、run-2B、run-2C與控制組之比較圖 圖3-8 run-2D之蘇力菌醱酵系統走勢圖 圖3-9 run-2A及run-2D與控制組之比較圖 圖3-10 run-2E之蘇力菌醱酵系統走勢圖 圖3-11 run-2E與run-1實驗組之比較圖 圖3-12 run-3A之蘇力菌醱酵系統走勢圖 圖3-13 run-3B之蘇力菌醱酵系統走勢圖 圖3-14 run-3A、run-3B與控制組的比較圖 圖3-15 run-2C、run-3B與控制組的比較圖 圖3-16 run-3C之蘇力菌醱酵系統走勢圖 圖3-17 run-3D之蘇力菌醱酵系統走勢圖 圖3-18 run-3C、run-3D與控制組的比較圖 圖3-19 run-4A之蘇力菌醱酵系統走勢圖 圖3-20 run-4B之蘇力菌醱酵系統走勢圖 圖3-21 run-4A、run-4B與控制組之比較圖 圖3-22 run-4C之蘇力菌醱酵系統走勢圖 圖3-23 run-4C與控制組之比較圖 圖3-24 氧氣質傳對產物生成的關係圖 圖3-25 run-5A之蘇力菌醱酵系統走勢圖 圖3-26 run-5B之蘇力菌醱酵系統走勢圖 圖3-27 run-5A、run-5B與控制組之比較圖 圖3-28 run-5C之蘇力菌醱酵系統走勢圖 圖3-29 run-5D之蘇力菌醱酵系統走勢圖 圖3-30 run-5C、run-5D與控制組之比較圖 圖3-31 最大剪應力對產物生成的關係圖

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