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  1. NTU Theses and Dissertations Repository
  2. 工學院
  3. 化學工程學系
請用此 Handle URI 來引用此文件: http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/29194
完整後設資料紀錄
DC 欄位值語言
dc.contributor.advisor邱文英
dc.contributor.authorChi-En Chouen
dc.contributor.author周琦恩zh_TW
dc.date.accessioned2021-06-13T01:02:40Z-
dc.date.available2012-07-26
dc.date.copyright2007-07-26
dc.date.issued2007
dc.date.submitted2007-07-23
dc.identifier.citation1. Huang T. Y., K. J. Duan, S. Y. Huang, and C. W. Chen, Production of polyhydroxyalkanoates from inexpensive extruded rice bran and starch by Haloferax mediterranei. J Ind Microbiol Biotechnol, 2006. 33: p. 701-706.
2. TSUGE, T., Metabolic Improvements and Use of Inexpensive Carbon Sources in Microbial Production of Polyhydroxyalkanoates. JOURNAL OF BIOSCIENCE AND BIOENGINEERING, 2002. 94(6): p. 579-584.
3. Khanna S., A. K. Srivastava, Recent advances in microbial polyhydroxyalkanoates. Process Biochemistry, 2005. 40: p. 607-619.
4. Sudesh K., H. Abe, and Y. Doi, Synthesis, structure and properties of polyhydroxyalkanoates: biological polyesters. Prog. Polym. Sci., 2000. 25: p. 1503-1555.
5. Lee, S. Y., Bacterial Polyhydroxyalkanoates. Biotechnology and Bioengineering, 1996. 49: p. 1-14.
6. Lenz R. W., and R. H. Marchessault, Bacterial Polyesters: Biosynthesis, Biodegradable Plastics and Biotechnology. Biomacromolecules, 2005. 6(1): p. 1-7.
7. Jose´ M Luengo , B. Garcia, A. Sandoval, G. Naharro, and E. R. Olivera, Bioplastics from microorganisms. Current Opinion in Microbiology, 2003. 6: p. 251-260.
8. Lee, S.Y., J. Choi, H. H. Wong, Recent advances in polyhydroxyalkanoate production by bacterial fermentation: mini-review. International Journal of Biological Macromolecules, 1999. 25: p. 31-36.
9. Witholt B. and B. Kessler, Perspectives of medium chain length poly(hydroxyaIkanoates), a versatile set of bacterial bioplastics. Environmental biotechnology, 1999. 10: p. 279-285.
10. Preusting H., A. Nijenhuis, and B. Witholt, Physical Characteristics of Poly( 3-hydroxyalkanoates) and Poly(3-hydroxyalkenoates) Produced by Pseudomonas oleouorans Grown on Aliphatic Hydrocarbons. Macromolecules, 1990. 23: p. 4220-4224.
11. Gross R. A., C. DeMello, and R. W. Lenz, Biosynthesis and Characterization of Poly@-hydroxyalkanoates) Produced by Pseudomonas oleovorans. Macromolecules, 1989. 22: p. 1106-1115.
12. Lee S. Y., H. H. Wong, J. Choi, S. H. Lee, S. C. Lee, and C. S. Han, Production of Medium-Chain-Length Polyhydroxyalkanoates by High-Cell-Density Cultivation of Pseudomonas putida Under Phosphorus Limitation. biotechnology and Bioengineering, 2000. 68(4): p. 466-470.
13. Sun Z., J. A. Ramsay, M. Guay, and B. A. Ramsay, Carbon-limited fed-batch production of medium-chain-length polyhydroxyalkanoates from nonanoic acid by Pseudomonas putida KT2440. Appl Microbiol Biotechnol, 2007. 74: p. 69-77.
14. Hazenberg W. and B. Witholt, Efficient production of medium-chain-length poly(3-hydroxyalkanoates) from octane by Pseudomonas oleovorans : economic considerations. Appl Microbiol Biotechnol, 1997. 48: p. 588-596.
15. Kim, B.S., Production of medium chain length polyhydroxyalkanoates by fed-batch culture of Pseudomonas oleovorans. Biotechnology Letters, 2002. 24: p. 125-130.
16. Kellerhals M. B., W. Hazenberg, and B. Witholt, High cell density fermentations of Pseudomonas oleovorans for the production of mcl-PHAs in two-liquid phase media. Enzyme and Microbial Technology, 1999. 24: p. 111-116.
17. Preusting H., R. Houten., A. Hoefs, E. K. Langenberghe, O. Favre-Bulle, and B. Witholt, High Cell Density Cultivation of Pseudomonas oleovorans: Growth and Production of Poly(3-hydroxyalkanoates) in Two-Liquid Phase Batch and Fed-Batch Systems. Biotechnology and Bioengineering, 1993. 41: p. 550-556.
18. Sudesh K., and Y. Doi, Molecular Design and Biosynthesis of Biodegradable Polyesters. Polym. Adv. Technol., 2000. 11: p. 865-872.
19. Zinn M., B. Witholt, and T. Egli, Occurrence, synthesis and medical application of bacterial polyhydroxyalkanoate. Advanced Drug Delivery Reviews, 2001. 53: p. 5-21.
20. Williams S. F., D. P. Martin, D. M. Horowitz, O. P. Peoples, PHA applications: addressing the price performance issue I. Tissue engineering. International Journal of Biological Macromolecules, 1999. 25: p. 111-121.
21. Chen G. Q., and Q. Wu, The application of polyhydroxyalkanoates as tissue engineering materials. Biomaterials, 2005. 26: p. 6565-6578.
22. Koning G., M. Kellerhals, C. Meurs, and B. Witholt, Poly(hydroxyalkanoates) from Fluorescent Pseudomonads in Retrospect and Prospect. Journal of Environmental Polymer Degradation, 1996. 4(4): p. 243-252.
23. 何宜靜, 利用Pseudomonas oleovorans生產含官能基之PHA及其結構與物性探討. 台灣大學碩士論文, 2006.
24. 楊勝斌, 以發酵法生產具官能基之聚酯材料. 台灣大學碩士論文, 2005.
25. Kim Y. B., R. W. Lenz, and R. C. Fuller, Poly-3-hydroxyalkanoates Containing Unsaturated Repeating Units Produced by Pseudomonas oleovorans. Journal of Polymer Science: Part A Polymer Chemistry, 1995. 33: p. 1367-1374.
26. Waard P., H. van der Wal, G. N. M. Huijberts, and G. Eggink, Heteronuclear NMR Analysis of Unsaturated Fatty Acids in Poly(3-hydroxyalkanoates). The Journal of Biological Chemistry, 1993. 268(1): p. 315-319.
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/29194-
dc.description.abstract本研究採用Pseudomonas oleovorans菌株發酵生產生物可分解性高分子,由於此菌株可合成出具中長碳鏈的PHA,性質較柔韌有彈性,與支鏈上短鏈長的PHB相較之下更具應用性。目前PHB已被大量生產,而具中長碳鏈之PHA(mcl-PHA, medium-chain-length PHA)由於產量低,仍未被加以探討,因此期望能夠提高mcl-PHA的產量。
使用辛酸鈉為碳源,硫酸銨為氮源,所產生的PHA為側鏈上具有五個碳的PHO(poly-3-hydroxyoctanoate)。發酵槽培養實驗中,當轉速提高時,溶氧量增加,使得菌體生長代謝加快,對數生長期提前結束。使用低溫培養,於16小時可得菌量4.43g/L,雖然菌量些微提升,但對於PHA累積量並沒有幫助。批次饋料培養,對數生長期延長,PHA產率降低。
錐形瓶饋加十一烯酸培養實驗,於培養40小時取樣可得最高菌量、最高PHA累積量分別為4.14g/L、2.148g/L,PHA含量可提升至51.8%。發酵槽饋加十一烯酸培養實驗,產物為PHO與PHU(poly-3-hydroxy-8-noneneoate為主)所形成之混摻物,且雙鍵所佔比例隨時間增加,培養第73小時可得到雙鍵比例37.39%;隨培養時間增加,玻璃轉移溫度(Tg, glass transition temperature)由-34.03℃下降至-42.40℃,顯示PHA性質變得更加柔韌具有彈性。
zh_TW
dc.description.abstractBiosynthesis of biodegradable PHA (polyhydroxyalkanoate) using Pseudomonas oleovorans was investigated. By using this microorganism, mclPHA can be synthesized. Comparing with sclPHA, the property of mclPHA is more flexible. To date only sclPHA have been synthesized at larger scale. Because of limited availability of the mclPHA, there are only a few reports on it.
Different products of PHA were obtained by using different carbon sources. When using sodium octanoate as a sole carbon source, major product was PHO (poly(3-hydroxyoctanoate)). Dissolved oxygen increases with higher stirrer speed, which promote metabolism of microorganism, logarithmic curve will end earlier. Change cultivation time from 30℃ to 18℃ at 8 hr can obtain 4.43g biomass/L, although dry cell weight was increased by a little, PHA accumulation was still too low. With fed-batch cultivation, PHA productivity is much lower than batch culture.
When feeding with undecylenic acid by flask culture, weight of PHA and PHA content were 2.148 g/L, 51.8% respectively. When feeding with undecylenic acid by fed-batch culture, there was a lag time when microorganism using undecylenic acid as a new carbon source. The molar fraction of unsaturated monomer could be achieved by 37.39% at 73 hr cultivation. We can see the property of PHA become flexible with cultivation time by the lower of Tg.
en
dc.description.provenanceMade available in DSpace on 2021-06-13T01:02:40Z (GMT). No. of bitstreams: 1
ntu-96-R94524026-1.pdf: 2856883 bytes, checksum: 991177cbe0835355bab8157bd6bb5dfa (MD5)
Previous issue date: 2007
en
dc.description.tableofcontents目錄
中文摘要 I
Abstract II
目錄 III
表目錄 VI
圖目錄 VIII
第一章 緒論 1
1-1前言 1
1-2研究目的 1
第二章 文獻回顧 2
2-1生物可分解性高分子簡介 2
2-2 PHA簡介 2
2-2.1 PHA結構 2
2-2.2 PHA性質 4
2-3 以Pseudomonas oleovorans發酵生產PHA 5
2-4 mcl-PHA的代謝路徑 6
2-5 未來發展與應用 10
第三章 材料與方法 11
3-1 實驗藥品與試劑 11
3-2 實驗儀器 13
3-3 實驗流程及方法 14
3-3.1 菌種來源 16
3-3.2 培養基組成 16
3-3.3 菌種活化與種菌培養 17
3-3.4 發酵槽操作流程 18
3-3.5 基質及產物之分析方法 20
3-3.5.1 銨氮濃度之測定 20
3-3.5.2 菌體乾重之測定 20
3-3.5.3 PHA之萃取與純化 20
3-3.5.4 核磁共振儀(NMR)分析 21
3-3.5.5 微差熱掃瞄分析儀(DSC)分析 21
3-3.5.6 凝膠滲透層析儀(GPC)分析 21
3-4 培養條件對於發酵槽批次(Batch)培養之影響 21
3-4.1 轉速影響之探討 21
3-4.2 溫度影響之探討 22
3-5 不同饋料策略對於批次饋料(Fed-Batch)培養之影響 22
3-5.1 饋入高濃度(NH4)2SO4且以辛酸鈉控制pH對於菌體累積之影響 22
3-5.2 添加低濃度(NH4)2SO4對於菌體累積之影響 22
3-5.3 添加辛酸鈉與(NH4)2SO4對於菌體累積之影響 23
3-6 饋入十一烯酸,對於PHA累積量以及結構之影響 23
3-6.1 錐型瓶培養於主培養後第16個小時饋入十一烯酸 23
3-6.2 發酵槽培養於第十小時饋入十一烯酸及硫酸銨 23
第四章 結果與討論 24
4-1 培養條件對於發酵槽批次(Batch)培養之影響 24
4-1.1轉速影響之探討 24
4-1.2溫度影響之探討 26
4-2不同饋料策略對於批次饋料(Fed-Batch)培養之影響 27
4-2.1 饋入高濃度(NH4)2SO4且以辛酸鈉控制pH對於菌體累積之影響 27
4-2.2 添加低濃度(NH4)2SO4對於菌體累積之影響 28
4-2.3 添加辛酸鈉與(NH4)2SO4對於菌體累積之影響 29
4-3饋入十一烯酸,對於PHA累積量以及結構組成之影響 31
4-3.1 錐型瓶培養於主培養後第16個小時饋入十一烯酸 31
4-3.2 發酵槽培養於第十小時饋入十一烯酸及硫酸銨 47
第五章 結論 64
參考文獻 65
附錄1 銨氮濃度標準曲線 68
dc.language.isozh-TW
dc.subjectPseudomonas oleovoranszh_TW
dc.subject聚羥基烷酯zh_TW
dc.subject批次饋料zh_TW
dc.subjectfed-batch cultureen
dc.subjectmclPHAen
dc.subjectPseudomonas oleovoransen
dc.subjectPolyhroxyalkanoatesen
dc.title利用Pseudomonas oleovorans生產具中長碳鏈之PHAzh_TW
dc.titleBiosynthesis of Medium-chain-length PHA by Pseudomonas oleovoransen
dc.typeThesis
dc.date.schoolyear95-2
dc.description.degree碩士
dc.contributor.coadvisor黃世佑
dc.contributor.oralexamcommittee董崇民,陳志成
dc.subject.keyword聚羥基烷酯,Pseudomonas oleovorans,批次饋料,zh_TW
dc.subject.keywordPolyhroxyalkanoates,Pseudomonas oleovorans,mclPHA,fed-batch culture,en
dc.relation.page67
dc.rights.note有償授權
dc.date.accepted2007-07-25
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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