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研究生: 侯泉福
Timothy
論文名稱: 增強結合反應蒸餾與萃取蒸餾於環己烷/異丙醇/水系統之模擬與控制
Enhanced Design and Control of Reactive and Extractive Distillation Processes for Cyclohexane/Isopropanol/Water Mixture
指導教授: 李豪業
Hao-Yeh Lee
口試委員: 游承修
Cheng-Hsiu Yu
余柏毅
Bor-Yih Yu
學位類別: 碩士
Master
系所名稱: 工程學院 - 化學工程系
Department of Chemical Engineering
論文出版年: 2023
畢業學年度: 111
語文別: 英文
論文頁數: 118
外文關鍵詞: Azeotropic separation, Heat integration
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Rapeseed oil has a wide range of uses in industries like automotive, chemical, biodiesel, and culinary. However, during its production, the leaching process generates a significant amount of waste that contains cyclohexane, isopropanol, and water. Due to the presence of several azeotropes and ternary azeotropes in this wastewater, it's crucial to develop an effective and energy-efficient treatment method. Six design alternatives are proposed and evaluated, including triple column extractive distillation (TCED), extractive distillation reactive distillation (EDRD), double column reactive-extractive distillation (DCRED), TCED with heat integration (TCED-HX), EDRD with heat integration (EDRD-HX), and DCRED with heat integration (DCRED-HX). The optimal configurations of each design are determined using the Simulated Annealing Algorithm (SAA) optimization technique. By combining reactive and extractive distillations, these designs offer the advantage of simultaneous chemical reactions and separation, leading to improved separation efficiency. The application of ethylene oxide (EO) as a dehydrating agent in reactive distillation columns enables the efficient removal of water from the mixture, reducing the number of required columns for separation. This innovative approach results in significant reductions in both capital and operating costs, ultimately leading to substantial reductions in the total annual cost (TAC). Compared with conventional configuration (TCED), the DCRED-HX has the optimal results. It can save 64.51% energy consumption and TAC up to 63.56%. Moreover, a control structure was developed for DCRED-HX to ensure the maintenance of product quality and process safety. Two control structures were proposed, and among them, control structure 2 was identified as the most effective at maintaining product purity under ±10% feed and composition disturbances.

ABSTRACT i ACKNOWLEDGEMENTS ii TABLE OF CONTENT iii LIST OF FIGURES v LIST OF TABLES viii CHAPTER 1 INTRODUCTION 1 1.1 Background 1 1.2 Literature Review 3 1.3 Motivation 9 1.4 Thesis Organization 10 CHAPTER 2 THERMODYNAMIC AND KINETIC MODELS 11 2.1 Thermodynamic Properties 11 2.1.1 Vapor-Liquid Equilibrium (VLE) 14 2.1.2 Liquid-Liquid Equilibrium (LLE) 17 2.2 Kinetic Model 20 CHAPTER 3 PROCESS DESIGNS AND THEIR OPTIMIZATIONS 21 3.1 Conventional Designs 21 3.1.1 Triple Column Extractive Distillation (Reproduce) 21 3.1.2 Triple Column Extractive Distillation with VLL Phase 27 3.2 Proposed Designs 33 3.2.1 Extractive Distillation Reactive Distillation (EDRD) 33 3.2.2 Double Column Reactive-Extractive Distillation (DCRED) 37 3.3 Optimization Method 40 3.3.1 Simulated Annealing Algorithm (SAA) 40 3.3.2 SAA Parameter Settings 44 3.4 Optimization of Conventional and Proposed Designs 47 3.4.1 Triple Column Extractive Distillation (TCED) 47 3.4.2 Extractive Distillation Reactive Distillation (EDRD) 55 3.4.3 Double Column Reactive-Extractive Distillation (DCRED) 63 3.5 Results and Discussions 70 CHAPTER 4 PROCESS DYNAMICS AND CONTROL PERFORMANCES 75 4.1 Double Column Reactive-Extractive Distillation with Heat Integrated (DCRED-HX) 78 4.1.1 DCRED-HX Control Scheme 1 (CS1) 78 4.1.2 DCRED-HX Control Scheme 2 (CS2) 87 4.2 Extractive Distillation Reactive Distillation with Heat Integrated (EDRD-HX) 94 4.2.1 EDRD-HX Control Scheme 1 (CS1) 94 4.2.2 EDRD-HX Control Scheme 2 (CS2) 100 4.2.3 EDRD-HX Control Scheme 3 (CS3) 104 4.2.4 Results and Discussions 108 CHAPTER 5 CONCLUSION AND FUTURE WORK 110 5.1 Conclusion 110 5.2 Future Work 111 REFERENCES 112 APPENDIX 116

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全文公開日期 2028/07/27 (校外網路)
全文公開日期 2028/07/27 (國家圖書館:臺灣博碩士論文系統)
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