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| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 吳哲夫 | zh_TW |
| dc.contributor.advisor | Jeffrey D. Ward | en |
| dc.contributor.author | 李佳穎 | zh_TW |
| dc.contributor.author | Chia-Yin Lee | en |
| dc.date.accessioned | 2025-09-10T16:18:25Z | - |
| dc.date.available | 2025-09-11 | - |
| dc.date.copyright | 2025-09-10 | - |
| dc.date.issued | 2025 | - |
| dc.date.submitted | 2025-07-30 | - |
| dc.identifier.citation | [1] A. A. Kiss, Advanced distillation technologies: design, control and applications. John Wiley & Sons, 2013.
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| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/99444 | - |
| dc.description.abstract | 儘管蒸餾的能耗高，但它仍然是分離揮發性混合物最廣泛使用的方法，每年約佔全球能源消耗的 3%。傳統的蒸餾程序存在重混效應，這會降低分離效率並增加能量需求。為了解決這些問題，雖然已提出如分隔壁塔（Dividing-Wall Columns, DWCs）等能量強化策略，但這些方法在控制上存在挑戰，尤其是在僅使用單一再沸器時需管理蒸氣分流。相比之下，堆疊複合蒸餾程序（或稱堆疊側線程序）透過側線抽取來減少重混效應，並藉由整合的再沸器-冷凝器熱交換器降低能耗。此設計不需蒸氣分流，但也帶來了新的控制挑戰：由於熱整合，系統失去了兩個控制自由度。值得注意的是，目前尚無針對堆疊側線程序控制性能的系統性研究。在本研究中，我們比較了傳統蒸餾程序、分隔壁塔與堆疊複合程序於等摩分離 BTX（三苯：苯、甲苯、二甲苯）時的動態控制行為。結果顯示，堆疊複合程序不僅具備優異的節能效果，亦展現出比分隔壁塔更佳的可控性，是一種具可行性與操作性的永續蒸餾設計方案。 | zh_TW |
| dc.description.abstract | Distillation remains the most widely used method for separating mixtures of volatile substances despite its high energy consumption, accounting for approximately 3% of global energy use annually. Traditional distillation sequences usually suffer from remixing effects that reduce separation efficiency and increase energy demand. The most widely-studied method for reducing the remixing effect is thermal coupling, including its embodiment as a dividing-wall column. Recently, however an alternative method called the stacked side-stream sequence has been shown to perform better in most cases. Dividing-wall columns face control challenges—particularly the need to manage vapor splits when only a single reboiler is used. A stacked side-stream sequence does not have a vapor split, but it introduces a different control challenge: the loss of two degrees of freedom due to thermal integration of a reboiler and a condenser. While hundreds of papers have been written on the control of dividing-wall columns, no prior studies have compared the control performance of stacked side-stream sequences with that of dividing-wall columns and conventional two-column sequences. Therefore, in this study, the dynamic control behavior of the conventional distillation sequence, the dividing-wall column, and the stacked side-stream sequence for the separation of BTX (benzene, toluene, xylene). Results show that the stacked side-stream sequence not only achieves superior energy savings but also demonstrates better controllability than the DWC, making it a promising option for sustainable and operable process design. | en |
| dc.description.provenance | Submitted by admin ntu (admin@lib.ntu.edu.tw) on 2025-09-10T16:18:25Z No. of bitstreams: 0 | en |
| dc.description.provenance | Made available in DSpace on 2025-09-10T16:18:25Z (GMT). No. of bitstreams: 0 | en |
| dc.description.tableofcontents | 口試委員會審定書 i
誌謝 ii 中文摘要 iii ABSTRACT iv CONTENTS v LIST OF FIGURES vii LIST OF TABLES xii Chapter 1 Introduction 1 1.1 Overview 1 1.2 Drawback of conventional sequence 2 1.3 Literature Review 4 1.4 Motivation 6 1.5 Method 7 Chapter 2 Process Design 9 2.1 Thermodynamic Validation 9 2.2 Conventional Distillation Sequence 10 2.3 Stacked Side-Stream Sequence 12 2.4 Dividing-Wall Column 15 Chapter 3 Control Strategies 20 3.1 Control of Conventional Distillation Sequence 20 3.2 Control of Stacked Side-Stream Sequence 24 3.2.1 Basic inventory control 25 3.2.2 Pressure-Compensated Temperature Strategy 28 3.2.3 Reboiler Level Cascade Strategy 33 3.3 Control of Dividing-Wall Column 37 Chapter 4 Results and Discussions 44 4.1 Conventional Distillation Sequence 45 4.2 Stacked Side-Stream Sequence 51 4.2.1 Pressure-Compensated Temperature Strategy 51 4.2.2 Reboiler Level Cascade Strategy 60 4.3 Dividing-Wall Column 68 4.3.1 Drawback of Dividing-Wall Column 75 4.4 Comparison of Three Different Distillation Sequences 77 Chapter 5 Conclusion 82 REFERENCES 83 | - |
| dc.language.iso | en | - |
| dc.subject | 堆疊式側線分離序列 | zh_TW |
| dc.subject | 製程控制 | zh_TW |
| dc.subject | 三苯 | zh_TW |
| dc.subject | 蒸餾 | zh_TW |
| dc.subject | 隔板塔 | zh_TW |
| dc.subject | BTX | en |
| dc.subject | Process control | en |
| dc.subject | Dividing-Wall Column | en |
| dc.subject | Stacked Side-stream Sequence | en |
| dc.subject | Distillation | en |
| dc.title | 三種不同蒸餾序列之控制策略開發 | zh_TW |
| dc.title | Control Strategy Development for Three Different Distillation Sequences | en |
| dc.type | Thesis | - |
| dc.date.schoolyear | 113-2 | - |
| dc.description.degree | 碩士 | - |
| dc.contributor.oralexamcommittee | 陳誠亮;李豪業 | zh_TW |
| dc.contributor.oralexamcommittee | Cheng-Liang Chen;Hao-Yeh Lee | en |
| dc.subject.keyword | 蒸餾,堆疊式側線分離序列,隔板塔,製程控制,三苯, | zh_TW |
| dc.subject.keyword | Distillation,Stacked Side-stream Sequence,Dividing-Wall Column,Process control,BTX, | en |
| dc.relation.page | 87 | - |
| dc.identifier.doi | 10.6342/NTU202502737 | - |
| dc.rights.note | 未授權 | - |
| dc.date.accepted | 2025-08-01 | - |
| dc.contributor.author-college | 工學院 | - |
| dc.contributor.author-dept | 化學工程學系 | - |
| dc.date.embargo-lift | N/A | - |
| 顯示於系所單位： | 化學工程學系 | |
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| ntu-113-2.pdf 未授權公開取用 | 6.42 MB | Adobe PDF |
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