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研究生: 黃宜鈞
Huang, Yi-Chun
論文名稱: 新型銅觸媒於低溫下降解苯乙烯
Innovative copper-based catalysts for the low-temperature catalytic oxidation of styrene
指導教授: 朱信
Chu, Hsin
學位類別: 碩士
Master
系所名稱: 工學院 - 環境工程學系
Department of Environmental Engineering
論文出版年: 2023
畢業學年度: 111
語文別: 英文
論文頁數: 169
中文關鍵詞: 低溫觸媒苯乙烯銅觸媒尖晶石結構固定床反應器反應動力
外文關鍵詞: Low-temperature catalyst, Styrene, Cu-based catalyst, Spinel structure, Fixed-bed reactor, Kinetics
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  • 觸媒氧化技術是現今富有潛力及經濟效益之VOCs處理技術,然而多半需要在高溫條件下才得以有效去除VOCs,若使用低溫觸媒可降低為達到高溫條件所衍生的龐大能源成本。銅質觸媒為極具優勢之低溫觸媒,因此開發出高效的銅質觸媒有其重要性。
    本研究藉由含浸法自製不同銅氧化物與氧化鋁比例的低溫觸媒,發現材料比例對觸媒的表面組成與結構有極大影響;並探討銅質觸媒於固定床反應器對苯乙烯的降解表現,以具尖晶石結構之10 wt%CuO/Al2O3觸媒的降解效果最佳。於操作參數實驗中,可發現10 wt%CuO/Al2O3觸媒對苯乙烯的降解效果隨苯乙烯濃度、空間速度或相對溼度增加而減少,且隨氧氣濃度增加而升高。衰化實驗中,觸媒於258oC以上時可維持高降解效率。研究中輔以TGA、XRD、XPS、SEM等精密儀器分析,佐證觸媒結構隨成分改變,並分析出觸媒反應前後之變化。另以MVK模式、L-H模式及E-R模式擬合以了解觸媒降解苯乙烯之反應動力。

    Catalytic oxidation using metal oxides is one of the promising and economical technologies for the reduction of volatile organic compounds (VOCs). However, most catalysts can only remove VOCs effectively under high-temperature conditions. The use of low-temperature catalysts can save considerable required energy costs. The application of copper-based catalyst low-temperature reaction is advantageous; therefore, the development of copper catalysts with high VOCs removal performance is essential.
    In this study, a series of low-temperature catalysts with various proportions of copper oxides to aluminum oxide were made by the impregnation method. It was noticed that the surface composition and structure of the catalyst would be strongly affected by the ratio of copper oxides and aluminum oxide. The catalytic efficiency of the copper catalysts for styrene removal was examined in a fixed-bed reactor, and the result showed that the 10 wt%CuO/Al2O3 catalyst with spinel structure exhibited the best performance. In the operating tests, the styrene removal efficiency of 10 wt%CuO/Al2O3 catalyst decreased under higher styrene concentration, space velocity, or relative humidity but elevated with increasing oxygen concentration. In the deactivation tests, the catalyst could maintain high catalytic efficiency when the operating temperature was above 258oC. Various instruments, such as TGA, XRD, XPS, and SEM, were also used to examine the structural difference among various prepared catalysts and to observe the change in the catalyst’s properties before and after the reaction. Furthermore, the kinetics of the catalyst for styrene removal would be fitted with MVK, L-H, and E-R model.

    摘要 I ABSTRACT II 致謝 III CONTENT V LIST OF TABLES IX LIST OF FIGURES XI CHAPTER 1 INTRODUCTION 1 1-1 Motivation 1 1-2 Objectives 2 CHAPTER 2 LITERATURE REVIEW 3 2-1 Volatile organic compounds (VOCs) 3 2-2 Styrene 4 2-3 VOCs control technologies 7 2-4 Catalytic oxidation 9 2-4.1 Introduction of catalytic oxidation 9 2-4.2 Reaction mechanisms of catalytic oxidation 10 2-4.3 Evaluation of catalytic efficiency 11 2-4.4 Influencing factors in the catalytic activity 12 2-5 Characteristics of the catalyst 15 2-5.1 Characteristics of aluminum oxides as support 15 2-5.2 Characteristics of copper oxide as metal oxides catalysts 15 2-6 Catalyst preparation methods 16 2-7 Catalyst deactivation 17 2-8 Catalytic kinetics 18 2-8.1 Plug flow reactor 19 2-8.2 Catalytic kinetics models 21 2-8.3 Arrhenius equation 27 CHAPTER 3 MATERIAL AND METHODS 28 3-1 Experimental methods 28 3-2 Experimental equipment 31 3-2.1 Experimental materials 31 3-2.2 Experimental instruments 31 3-2.3 Experimental facilities 34 3-2.4 Analytical instruments 37 3-3 Preliminary experiment 39 3-3.1 Catalyst preparation 39 3-3.2 Leakage proof 40 3-3.3 Calibration curve 40 3-3.4 Stability test 41 3-4 Catalytic activity test 42 3-5 Operating parameter tests 43 3-5.1 Styrene concentration 43 3-5.2 Space velocity 43 3-5.3 Oxygen concentration 44 3-5.4 Relative humidity (RH) 44 3-6 Cyclic operation test 44 3-7 Deactivation test 44 3-8 Study of reaction kinetics 45 3-9 Reaction mechanism 45 3-9.1 Mineralization of the reaction 45 CHAPTER 4 RESULTS AND DISCUSSION 47 4-1 Characterizations of catalysts 47 4-1.1 Inductively Coupled Plasma-Optical Emission Spectrometer (ICP-OES) 47 4-1.2 Thermogravimetric analysis (TGA) 48 4-1.3 X-ray diffraction (XRD) analysis 53 4-1.4 Scanning electron microscopy (SEM) 62 4-1.5 Scanning electron microscopy with energy dispersive spectroscopy (SEM-EDS) and mapping analysis 66 4-1.6 Transmission electron microscopy (TEM) 76 4-1.7 Brunauer-Emmett-Teller (BET) surface area analysis 82 4-1.8 Fourier transform infrared (FTIR) analysis 86 4-1.9 X-ray photoelectron spectroscopy (XPS) 88 4-2 Catalytic activity tests 95 4-2.1 Metal loading effect 96 4-2.2 Styrene concentration 99 4-2.3 Space velocity 101 4-2.4 Oxygen concentration 103 4-2.5 Relative humidity 105 4-2.6 Cyclic operation test 107 4-2.7 Deactivation test 109 4-3 Characterizations of fresh and spent catalysts 110 4-3.1 X-ray diffraction (XRD) analysis 111 4-3.2 Scanning electron microscopy (SEM) 114 4-3.3 Scanning electron microscopy with energy dispersive spectroscopy (SEM-EDS) and mapping analysis 116 4-3.4 Transmission electron microscopy (TEM) 123 4-3.5 Thermogravimetric analysis (TGA) 128 4-3.6 Elemental analysis (EA) 133 4-3.7 Brunauer-Emmett-Teller (BET) surface area analysis 134 4-3.8 Fourier transform infrared (FTIR) analysis 137 4-3.9 X-ray photoelectron spectroscopy (XPS) 139 4-4 Kinetics study 144 4-5 Reaction mechanism 151 4-5.1 Mineralization of the reaction 151 CHAPTER 5 CONCLUSION AND SUGGESTION 153 5-1 Conclusion 153 5-2 Suggestions 155 REFERENCES 156

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