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| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 吳哲夫(Jeffrey D. Ward) | |
| dc.contributor.author | Wei-En Lin | en |
| dc.contributor.author | 林煒恩 | zh_TW |
| dc.date.accessioned | 2021-06-16T13:21:43Z | - |
| dc.date.available | 2020-06-24 | |
| dc.date.copyright | 2020-06-24 | |
| dc.date.issued | 2020 | |
| dc.date.submitted | 2020-06-19 | |
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| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/61983 | - |
| dc.description.abstract | 在本篇論文中，利用模擬最適化並以年總成本為目標函數，比較三成分無共沸物系統之分離程序，共有七種分離程序做比較：直接序列設計、直接序列設計搭配堆疊整合、間接序列設計、間接序列設計搭配堆疊整合以及三種內隔壁式蒸餾塔，所有分離程序皆是使用嚴謹程序模擬，並利用模擬退火演算法做最適化。 在結果呈現中，運用三元相圖表示不同進料組成之最適分離程序，此外，以所有數據回歸出為進料組成、相對揮發度、分離難度指標函數之模型，此模型可用於預測未知系統，若擁有未知系統之進料組成與其相對揮發度，便可預測其最適分離程序。 本篇論文結果指出堆疊整合於分離三成分系統之重要性，當考慮堆疊整合之應用時，許多進料組成之最適分離程序，相較於不考慮堆疊整合時，都更傾向於使用直接序列設計搭配堆疊整合或間接序列設計搭配堆疊整合，而非使用內隔壁式蒸餾塔。 | zh_TW |
| dc.description.abstract | Alternatives for separation of three-component zeotropic mixtures are compared using simulation-optimization with total annual cost as the objective function. Conventional two-column sequences with and without column stacking are compared with three types of dividing-wall columns (DWCs). All processes are modeled with a rigorous process simulator and optimized using simulated annealing algorithm (SA). The results are represented using ternary maps and used to regress parameters of a model that predicts the relative cost of process alternatives as a function of the feed composition, relative volatilities (α) and ease of separation index (ESI). The results highlight the importance of considering column stacking when choosing a process alternative for ternary separation: In some cases, the region where the stacked two-column configuration is preferable to a dividing-wall column is significantly larger than the area where a conventional two-column configuration is preferable to a dividing-wall column. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-16T13:21:43Z (GMT). No. of bitstreams: 1 U0001-1806202017031400.pdf: 3397838 bytes, checksum: 5bfa9dae3931af50b4949e3c96c06a9e (MD5) Previous issue date: 2020 | en |
| dc.description.tableofcontents | Table of Contents
口試委員會審定書 ii 謝辭 iii 中文摘要及關鍵詞 iv Abstract v Table of Contents vi List of Figures x List of Tables xiii 1. Introduction 1 2. Methods 3 2.1. Column Sequencing with Column Stacking 7 2.2. DWCs 10 2.3. Optimization Method 12 2.3.1. SA Overview 13 2.3.2. SA Parameters 15 2.3.3. SA Flowchart 17 2.4. Representation of Results 19 2.4.1. Regression for Individual Ternary Mixtures 20 2.4.2. α and ESI 22 2.5. Contour Map 23 2.6. Case Studies 24 2.6.1. Ethanol / 1-Propanol / 1-Butanol (EPB) 24 2.6.2. N-Butane / I-Pentane / N-Pentane (BPP) 25 2.6.3. N-Heptane/Toluene/O-Xylene (HTX) 26 3. Results 27 3.1. EPB System 27 3.2. BPP System 38 3.3. HTX System 48 3.4. Regression including α and ESI 58 4. Conclusions 62 References 64 Appendix A. TAC Calculation 72 1. Column Capital Cost 72 2. Condenser Capital Cost 72 3. Condenser Energy Cost 73 4. Reboiler Capital Cost 73 5. Reboiler Energy Cost 74 6. Heat Exchanger Capital Cost 74 7. Vacuum System Capital Cost and Energy Cost 77 8. TAC 79 Appendix B. Optimized Process Design Variables 80 1. Nomenclature 80 2. Optimized Process Design Variables for D for EPB System 84 3. Optimized Process Design Variables for DH for EPB System 85 4. Optimized Process Design Variables for I for EPB System 86 5. Optimized Process Design Variables for IH for EPB System 87 6. Optimized Process Design Variables for DWCL for EPB System 88 7. Optimized Process Design Variables for DWCM for EPB System 89 8. Optimized Process Design Variables for DWCU for EPB System 90 9. Optimized Process Design Variables for D for BPP System 91 10. Optimized Process Design Variables for DH for BPP System 92 11. Optimized Process Design Variables for I for BPP System 93 12. Optimized Process Design Variables for IH for BPP System 94 13. Optimized Process Design Variables for DWCL for BPP System 95 14. Optimized Process Design Variables for DWCM for BPP System 96 15. Optimized Process Design Variables for DWCU for BPP System 97 16. Optimized Process Design Variables for D for HTX System 98 17. Optimized Process Design Variables for DH for HTX System 99 18. Optimized Process Design Variables for I for HTX System 100 19. Optimized Process Design Variables for IH for HTX System 101 20. Optimized Process Design Variables for DWCL for HTX System 102 21. Optimized Process Design Variables for DWCM for HTX System 103 22. Optimized Process Design Variables for DWCU for HTX System 104 | |
| dc.language.iso | en | |
| dc.subject | 最適化 | zh_TW |
| dc.subject | 直接序列設計 | zh_TW |
| dc.subject | 堆疊整合 | zh_TW |
| dc.subject | 內隔壁式蒸餾塔 | zh_TW |
| dc.subject | 模擬退火演算法 | zh_TW |
| dc.subject | 間接序列設計 | zh_TW |
| dc.subject | ease of separation index | en |
| dc.subject | direct sequence | en |
| dc.subject | indirect sequence | en |
| dc.subject | column stacking | en |
| dc.subject | dividing-wall column | en |
| dc.subject | simulated annealing algorithm | en |
| dc.subject | regions of optimality | en |
| dc.title | 利用嚴謹模擬、隨機最適化與蒸餾塔熱整合辨別最適分離程序 | zh_TW |
| dc.title | Regions of Optimality for Separation System Synthesis Using Rigorous Modeling, Stochastic Optimization and Column Stacking | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 108-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 錢義隆(I-Lung Chien),陳誠亮(Cheng-Liang Chen),李豪業(Hao-Yeh Lee) | |
| dc.subject.keyword | 直接序列設計,間接序列設計,堆疊整合,內隔壁式蒸餾塔,模擬退火演算法,最適化, | zh_TW |
| dc.subject.keyword | direct sequence,indirect sequence,column stacking,dividing-wall column,simulated annealing algorithm,regions of optimality,ease of separation index, | en |
| dc.relation.page | 104 | |
| dc.identifier.doi | 10.6342/NTU202001051 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2020-06-19 | |
| 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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