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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 | Te-Yu Tsai | en |
dc.contributor.author | 蔡德諭 | zh_TW |
dc.date.accessioned | 2021-06-16T10:48:45Z | - |
dc.date.available | 2020-07-17 | |
dc.date.copyright | 2020-07-17 | |
dc.date.issued | 2020 | |
dc.date.submitted | 2020-07-01 | |
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dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/61138 | - |
dc.description.abstract | 本篇提出一方法可對分離勻相共沸混合物自動生成,並最適化可行塔序列。此方法包含依前人所提出之方法分析共沸混合物性質及產生可行塔序列,和以模擬退火法最適化各序列中各個蒸餾塔之年度總成本(TAC),並主要於Python及Aspen Plus實現程序模擬及自動化,節省以往繁複的手續所需時間與人力,以期發掘最佳之塔序列設計。此方法用以探討含三個兩相共沸物之五成份混合物,乙酸甲酯(methyl acetate)/甲醇(methanol)/乙醇(ethanol)/水(water)/乙酸(acetic acid),及含一兩相共沸物之四成份混合物,丙酮(acetone)/氯仿(chloroform)/苯(benzene)/甲苯(toluene)。 | zh_TW |
dc.description.abstract | A method is developed for determining feasible sequences for separating mixtures with binary azeotropes and optimizing each column in every sequence (including two-column subsequences for azeotropic distillation and solvent recovery) to determine which sequence has the lowest overall cost. The method can be applied automatically for different feed mixtures and feed compositions, which permits screening of process alternatives including different feed compositions. The results are illustrated using two case study systems: a five-component mixture with three binary azeotropes and one distillation region and a four-component mixture with one binary azeotrope and two distillation regions. | en |
dc.description.provenance | Made available in DSpace on 2021-06-16T10:48:45Z (GMT). No. of bitstreams: 1 U0001-3006202021070200.pdf: 2284960 bytes, checksum: cfd7a77956d0ba633812c96389207097 (MD5) Previous issue date: 2020 | en |
dc.description.tableofcontents | 論文委員口試審定書 i 誌謝 ii 摘要 iii Abstract iv Table of Contents v List of Figures viii List of Tables x 1. Introduction 1 2. Methodology 5 2.1. Identification of feasible sequences 5 2.1.1. Topological analysis 5 2.1.2. Split selection 8 2.1.3. Generation of feasible sequences 12 2.2. Column design and optimization 17 2.2.1. Simulated annealing algorithm 17 2.2.2. Ordinary distillation columns 24 2.2.3. Two-column extractive distillation subsystems 25 2.3. Implementation of automation 26 2.3.1. Access to Aspen Properties in external programs 27 2.3.2. ActiveX automation server with Aspen Plus 29 2.3.3. Preliminary preparation 29 3. Results 31 3.1. Five-component mixture of methyl acetate, methanol, ethanol, water and acetic acid 31 3.1.1. Overview 31 3.1.2. Equimolar feed (0.2/0.2/0.2/0.2/0.2) 34 3.1.3. 0.15/0.3/0.1/0.15/0.3 42 3.2. Four component mixture of acetone, chloroform, benzene and toluene 49 3.2.1. Overview 49 3.2.2. Equimolar feed (0.25/0.25/0.25/0.25) 52 3.2.3. 0.1/0.1/0.4/0.4 60 4. Conclusions 65 5. References 66 Appendix A: Total annual cost calculation 73 | |
dc.language.iso | zh-TW | |
dc.title | 自動塔序列最適化於勻相共沸混合物 | zh_TW |
dc.title | Automatic Column Sequencing and Optimization for Homogeneous Azeotropic Mixtures | 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 | 塔序列,共沸混合物,模擬退火法,最適化,自動化, | zh_TW |
dc.subject.keyword | column sequencing,azeotropic mixture,simulated annealing algorithm,optimization,automation, | en |
dc.relation.page | 77 | |
dc.identifier.doi | 10.6342/NTU202001222 | |
dc.rights.note | 有償授權 | |
dc.date.accepted | 2020-07-01 | |
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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