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完整後設資料紀錄
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dc.contributor.advisor劉懷勝
dc.contributor.authorYung-Chen Chanen
dc.contributor.author詹詠臻zh_TW
dc.date.accessioned2021-06-16T13:03:09Z-
dc.date.available2015-08-08
dc.date.copyright2013-08-08
dc.date.issued2013
dc.date.submitted2013-08-06
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謝榕庭 (2010) 以Gluconacetobater xylinus生產細菌纖維素之研究. 國立台灣大
學化學工程學研究所, 台灣大學. 碩士
黃翔瑜 (2010) 以Gluconacetobater xylinus連續式生產細菌纖維素薄膜之研究.國立台灣大學化學工程學研究所, 台灣大學. 碩士
林政勛 (2012) 以Gluconacetobater xylinus連續生產細菌纖維素之反應器設計與操作. 國立台灣大學化學工程學研究所, 台灣大學. 碩士
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/61444-
dc.description.abstractBacterial cellulose (BC) is a kind of polysaccharide produced by particular strains, and it can be applied to many fields such as paper industry, food industry and biomedical materials. In contrast to plant cellulose, it has unique nano-network structure and physicochemical properties. The fed-batch process of static culture to produce BC pellicles showed that the thickness of BC pellicles was well-controlled almost infinitely with higher productivity. The production rate was maintained only under sufficient nutrients and oxygen. A fed-batch operation was to supply fresh medium on the top of BC pellicles already formed to permit the continuation of bacterial growths. In the same period of 30 days, by the fed-batch process, BC pellicles reached to a thickness of 20~40 mm, that was at least ten times of the traditional conventional static culture. In addition, by controlling the liquid height of medium added to the top of BC pellicles, the continuity between new BC pellicle and the old one was controlled. If the height was less than 1mm, the added medium the previously formed pellicle would become ‘one’ thick BC pellicle. Otherwise, it became a layer-by-layer pellicles formation process. With glucose diffusion experiments to measure the permeability of BC pellicles, similar permeability coefficient (7.735×10-6 cm2/s) for either fed-batch or conventional static process was discovered, independent of their thickness. However, the thick BC pellicle was packed so loosely that the permeability coefficient increased to 1.233×10-5(cm2/s) because of less mechanical stability. This difference was also controlled by the liquid height of medium added.en
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dc.description.tableofcontents口試委員審定書 ............................................. I
謝誌 .................................................... II
摘要 ................................................... III
Abstract ................................................ IV
第一章 緒論 ............................................... 1
第二章 文獻回顧 ............................................ 3
2.1 細菌纖維素介紹 ......................................... 3
2.1.1 細菌纖維素的基本結構 .................................. 3
2.1.2 細菌纖維素的理化性質 .................................. 6
2.1.3 細菌纖維素的特性 ...................................... 8
2.1.4 細菌纖維素的應用 ..................................... 12
2.2 細菌纖維素生產菌株 ..................................... 16
2.2.1 Acetobacter xylinum的生理特性 ...................... 17
2.2.2 細菌纖維素的合成 ..................................... 20
2.2.3 細菌纖維素合成酶的調控機制 ............................ 27
2.2.4 影響細菌纖維素生成的因素 .............................. 29
2.3 細菌纖維素薄膜的通透性 .................................. 52
第三章 實驗流程、方法、藥品及儀器 ............................. 58
3.1 實驗菌株 ............................................. 58
3.2 培養基組成 ........................................... 59
3.3 實驗方法 ............................................. 61
3.3.1 預培養 ............................................. 61
3.3.2 主培養 ............................................. 62
3.3.3 產物處理 ........................................... 62
3.3.4 以DNS試劑測還原糖濃度 ................................ 63
3.3.5 擴散實驗 ........................................... 65
3.4 實驗藥品 ............................................. 66
3.5 實驗儀器 ............................................. 66
第四章 實驗結果與討論 ...................................... 67
4.1 培養基體積(液高)對於饋料批次靜置培養細菌纖維素的影響 ......... 69
4.1.1培養基體積(液高)對於培養時間的影響 ....................... 69
4.1.1.1 批次靜置實驗中培養基體積(液高)對於培養時間的影響 ........ 69
4.1.1.2 饋料批次靜置培養第二週期培養基添加體積(液高)對於培養時間的影響 ........................................................ 73
4.1.2 饋料批次靜置培養第二週期後重覆添加培養基體積(液高)對於分層的影響 ........................................................ 75
4.2 饋料批次靜置培養厚度間的關係 ............................. 80
4.2.1初始培養基體積對於厚度增加的影響 ......................... 80
4.2.2重覆添加培養基體積對於厚度增加的影響 ..................... 82
4.2.2.1 重覆添加培養基間隔時間為十二小時 ..................... 82
4.2.2.2 重覆添加培養基間隔時間為二十四小時 .................... 89
4.2.3培養容器大小對於厚度的影響 ............................. 96
4.2.4饋料批次靜置培養對於Gluconacetobacter xylinus生成纖維素產量的影響 ................................................... 109
4.3 細菌纖維素薄膜對於葡萄糖的通透性 ........................ 113
4.3.1 單層薄膜擴散實驗 ................................... 114
4.3.2 雙層薄膜及兩倍厚度薄膜擴散實驗 ........................ 117
4.3.3 三層薄膜及三倍厚度薄膜擴散實驗 ........................ 123
4.3.4 結果整理 .......................................... 127
第五章 結論 ............................................. 129
參考文獻 ................................................ 132
dc.language.isozh-TW
dc.subject細菌纖維素zh_TW
dc.subject饋料批次zh_TW
dc.subject通透性zh_TW
dc.subjectbacterial celluloseen
dc.subjectfed-batchen
dc.subjectpermeabilityen
dc.title以Gluconacetobacter xylinus饋料批次靜置生產細菌纖維素之研究zh_TW
dc.titleFed-batch Production of Bacterial Cellulose in Static Conditions by Gluconacetobacter xylinusen
dc.typeThesis
dc.date.schoolyear101-2
dc.description.degree碩士
dc.contributor.oralexamcommittee賴進此,許駿發,王孟菊
dc.subject.keyword細菌纖維素,饋料批次,通透性,zh_TW
dc.subject.keywordbacterial cellulose,fed-batch,permeability,en
dc.relation.page139
dc.rights.note有償授權
dc.date.accepted2013-08-06
dc.contributor.author-college工學院zh_TW
dc.contributor.author-dept化學工程學研究所zh_TW
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