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完整後設資料紀錄
DC 欄位 | 值 | 語言 |
---|---|---|
dc.contributor.advisor | 吳哲夫(Jeffrey D. Ward) | |
dc.contributor.author | Chuan-Chen Chao | en |
dc.contributor.author | 趙傳真 | zh_TW |
dc.date.accessioned | 2021-05-20T20:56:55Z | - |
dc.date.available | 2014-08-03 | |
dc.date.available | 2021-05-20T20:56:55Z | - |
dc.date.copyright | 2011-08-03 | |
dc.date.issued | 2011 | |
dc.date.submitted | 2011-07-28 | |
dc.identifier.citation | [1] Wright, R.O. and N.J.Elizabeth, 'Fractional apparatus'. 1949. US Patent, 2,471,134
[2] Wolff, E.A. and S. Skogestad, 'Operation of integrated 3-product (Petlyuk) distillation-columns'. Ind. Eng. Chem. Res., 1995. 34: p. 2094-2103. [3] Mutalib, M.I.A. and R. Smith, 'Operation and control of dividing wall distillation columns - Part 1: Degrees of freedom and dynamic simulation'. Chem. Eng. Res. Des., 1998. 76: p. 308-318. [4] Mutalib, M.I.A., A.O. Zeglam, and R. Smith, 'Operation and control of dividing wall distillation columns - Part 2: Simulation and pilot plant studies using temperature control'. Chem. Eng. Res. Des, 1998. 76: p. 319-334. [5] Serra, M., Espun˜a, A., and Puigjaner, L. 'Control and optimization of the divided wall column'. Chemical Engineering and Processing, 1999, 38: p.549–562. [6] Serra, M.; Espun˜a, A.; Puigjaner, L. 'Study of the divided wall column controllability: influence of design and operation'. Comput. Chem. Eng. 2000, 24: p.901. [7] Halvorsen, I.J. and S. Skogestad, 'Optimal operation of Petlyuk distillation: steady-state behavior'. Journal of Process Control, 1999. 9: p. 407-424. [8] Serra, M., M. Perrier, A. Espuna, and L. Puigjaner, 'Analysis of different control possibilities for the divided wall column: feedback diagonal and dynamic matrix control'. Comput. Chem. Eng., 2001. 25: p. 859-866. [9] Serra, M., A. Espuna, and L. Puigjaner, 'Controllability of different multicomponent distillation arrangements'. Ind. Eng. Chem. Res., 2003. 42: p. 1773-1782. [10] Adrian, T., H. Schoenmakers, and M. Boll, 'Model predictive control of integrated unit operations: Control of a divided wall column'. Chem. Eng. Process., 2004. 43: p. 347-355. [11] Wang, S.J. and D.S.H. Wong, 'Controllability and energy efficiency of a high-purity divided wall column'. Chem. Eng. Sci., 2007. 62: p. 1010-1025. [12] Cho, Y., B. Kim, D. Kim, M. Han, and M. Lee, 'Operation of divided wall column with vapor sidedraw using profile position control'. Journal of Process Control, 2009. 19: p. 932-941. [13] Ling, H. and W.L. Luyben, 'New control structure for divided-wall columns'. Ind. Eng. Chem. Res., 2009. 48: p. 6034-6049. [14] R.C. Van Diggelen, A.A. Kiss, A.W. Heemink, 'Comparison of control strategies for dividing-wall columns'. Industrial & Engineering Chemistry Research, 2010,49: p.288-307. [15] Anton A. Kiss, Costin Sorin Bildea, 'A control perspective on process intensification in dividing-wall columns'. Chemical Engineering and Processing, 2011, 50: p.281-292 [16] 黃琦聰(Huang)、黃聖夫、方淞, 『分隔內壁蒸餾塔簡介』 《化工技術》 第14 卷第7 期 (2006 年7 月號), p.105-113 [17] Kai-Ti Chu, 'Steady state design and economic analysis of divided wall column'. Department of Chemical Engineering College of Engineering National Taiwan University Master Thesis, 2010, 6 [18] Underwood, A.J.V., 'Fractional distillation of multicomponent mixtures'. Chem. Eng. Prog., 1948. 44: p. 603-614. [19] Halvorsen, I.J. and S. Skogestad, 'Minimum energy consumption in multicomponent distillation. 2. Three-product Petlyuk arrangements'. Ind. Eng. Chem. Res., 2003. 42: p. 605-615. [20] Gilliland, E.R., 'Multicomponent rectification - Estimation of the number of theoretical plates as a function of the reflux ratio'. Ind. Eng. Chem., 1940. 32: p. 1220-1223. [21] C. G. Kirkbride, 'Process design procedure for multicomponent fractionators '. Pet. Ref. 1944, 23, 321. [22] Bristol, E. H., 'On a new measure of interaction for multivariable process control'. IEEE Trans. Auto. Control, AC-11, 1966. 133 [23] Dale E. Seborg, Thomas F. Edgar, Duncan A. Mellichamp, 'Process dynamics and control'.Wiley: New Jersey, 2004 [24] McAvoy, T. J., Interaction Analysis, ISA, Research Triangle Park, NC, 1983 [25] Sigurd Skogestad, Ian Postlethwaite, 'Multivariable feedback control'. Wiley: New York, 1996 | |
dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/10030 | - |
dc.description.abstract | 相較於傳統的蒸餾序列,內隔壁式蒸餾塔 (DWC) 是一種在分離多成分混合物時,可以節省更多的能量與設備成本的前瞻性設計。然而,內隔壁式蒸餾塔在設計上也較為困難,因為較傳統序列擁有更多的設計自由度。約莫五十年前,內隔壁式蒸餾塔的設計方法被提出討論,許多論文討論穩態設計問題,並提出啟發式和嚴謹的設計優化方法。但是,內隔壁式蒸餾塔的控制相對的得到較少的關注。此研究主要是針對內隔壁式蒸餾塔分離理想系統的可控性進行調查。對於不同類型的內隔壁式蒸餾塔、不同相對揮發度的分離指標、不同的進料條件,進行可控性的分析。並對於不同的控制策略,採用線性分析工具,相對增益陣列 (RGA) 和條件數 (CN) 進行分析。論文中為符合實際工廠使用的控制策略,利用進料擾動從動態上測試其排除干擾的能力。最後,從控制的角度提出一選擇何種類型內隔壁式蒸餾塔之指導方針。 從控制的觀點發現,當進料含有較多輕成分時建議使用上隔板式蒸餾塔;當進料含有較多中間成分時建議使用下隔板式蒸餾塔;當進料含有較多重成分時建議使用上隔板式蒸餾塔。 | zh_TW |
dc.description.abstract | The divided-wall column system is a promising energy saving alternative for separating multi-component mixtures compared with traditional distillation columns. However the design of DWCs is more difficult because there are more degrees of freedom. The control of the DWC have received much less attention. In this work, the controllability of a divided wall column for separating ideal system were investigated. The main objective of this work is to study the divided-wall column (DWC) controllability. A controllability analysis of the ideal system is done for the separation of different types of DWC, different ease separation index (ESI) and different feed condition. Different control structures are compared using linear analysis tools, relative gain array (RGA) and condition number (CN). Disturbances in feed fowrate and feed composition are used to demonstrate the effectiveness of the proposed control structure. Finally, a guideline for the selection of the divided-wall column is proposed. Based on control considerations for different feed conditions, it is found that: If there is more lightest component in the feed, DWCU is preferred. If there is more middle component in the feed, DWCL is preferred. If there is more heaviest component in the feed, DWCU is preferred. | en |
dc.description.provenance | Made available in DSpace on 2021-05-20T20:56:55Z (GMT). No. of bitstreams: 1 ntu-100-R98524020-1.pdf: 4303335 bytes, checksum: 7cb5ea998a9cfd313429ede2a0ba877e (MD5) Previous issue date: 2011 | en |
dc.description.tableofcontents | 誌謝 i
摘要 iii Abstract v Table of Contents vii List of Figures xi List of Tables xix 1 Introduction 1 1.1 Preface 1 1.2 Introduction for DWCs 4 1.2.1 DWCL 4 1.2.2 DWCU 5 1.2.3 DWCM 7 1.3 Literature survey 9 1.4 Motivation 13 1.5 Thesis organization 14 2 Steady-State Analysis 15 2.1 Thermodynamic properties 15 2.2 Shortcut method 18 2.3 Analysis method 26 2.3.1 Relative Gain Array 26 2.3.2 Condition Number 29 2.4 Results 30 2.4.1 DWCL 31 2.4.2 DWCU 44 2.4.3 DWCM 45 2.5 Summary 58 3 Dynamic Analysis 63 3.1 Dynamic simulation 63 3.2 Analysis method 65 3.2.1 Integral Error Criteria 65 3.3 Results of feed flowrate disturbance 66 3.3.1 DWCL 66 3.3.2 DWCU 83 3.3.3 DWCM 97 3.4 Results of feed composition disturbance 116 3.5 Summary 118 4 Conclusion 123 Appendix A 129 Reference 135 | |
dc.language.iso | en | |
dc.title | 內隔壁式蒸餾塔之動態與控制 | zh_TW |
dc.title | Dynamics and Control of Divided Wall Columns | en |
dc.type | Thesis | |
dc.date.schoolyear | 99-2 | |
dc.description.degree | 碩士 | |
dc.contributor.oralexamcommittee | 錢義隆,陳誠亮 | |
dc.subject.keyword | 內隔壁式蒸餾,控制,相對增益陣列, | zh_TW |
dc.subject.keyword | divided-wall column,control,relative gain array, | en |
dc.relation.page | 137 | |
dc.rights.note | 同意授權(全球公開) | |
dc.date.accepted | 2011-07-28 | |
dc.contributor.author-college | 工學院 | zh_TW |
dc.contributor.author-dept | 化學工程學研究所 | zh_TW |
顯示於系所單位: | 化學工程學系 |
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