請用此 Handle URI 來引用此文件:
http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/99444| 標題: | 三種不同蒸餾序列之控制策略開發 Control Strategy Development for Three Different Distillation Sequences |
| 作者: | 李佳穎 Chia-Yin Lee |
| 指導教授: | 吳哲夫 Jeffrey D. Ward |
| 關鍵字: | 蒸餾,堆疊式側線分離序列,隔板塔,製程控制,三苯, Distillation,Stacked Side-stream Sequence,Dividing-Wall Column,Process control,BTX, |
| 出版年 : | 2025 |
| 學位: | 碩士 |
| 摘要: | 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。 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. |
| URI: | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/99444 |
| DOI: | 10.6342/NTU202502737 |
| 全文授權: | 未授權 |
| 電子全文公開日期: | N/A |
| 顯示於系所單位: | 化學工程學系 |
文件中的檔案:
| 檔案 | 大小 | 格式 | |
|---|---|---|---|
| ntu-113-2.pdf 未授權公開取用 | 6.42 MB | Adobe PDF |
系統中的文件,除了特別指名其著作權條款之外,均受到著作權保護,並且保留所有的權利。
