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研究生: 李瑀軒
Yu-Hsuan Li
論文名稱: 在管柱中以活性碳吸附與脫附異丙醇水溶液行為之研究
Adsorption and Desorption Study of Isopropyl Alcohol Aqueous Solution with Activated Carbon in the Fixed-bed Column
指導教授: 曾堯宣
Yao-Hsuan Tseng
顧 洋
Young Ku
口試委員: 蔣本基
Pen-Chi Chiang
曾迪華
Dyi-Hwa Tseng
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: 2018
畢業學年度: 106
語文別: 英文
論文頁數: 127
中文關鍵詞: 活性碳異丙醇蒸氣再生廢活性碳活性碳管柱吸附脫附
外文關鍵詞: activated carbon, isopropyl alcohol, steam regeneration, fixed-bed column adsorption, desorption
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  • 隨著科技的發展,光電科技產業竄升為台灣之重點科技之一。然而,在科技快速發展的同時,也伴隨著環境污染,其中最受影響的污染為水資源的消耗。在廢水處理技術中,對含有低濃度之有機物或毒性物質,多透過活性碳吸附作用去除,使水資源得以回到原製程使用。然而,若活性碳達到吸附飽和則失去原本的吸附能力,無法在去除水中污染物。因此開發廢活性碳再生技術,延長活性碳的使用壽命,減少活性碳吸附程序的操作成本,不僅能降低產業營運成本提高收益,亦能減少環境破壞,達成循環經濟之目標。
    本研究中,以異丙醇作為活性碳吸附與脫附的污染物。在管柱吸附異丙醇水溶液研究前,進行批次吸附研究以確定活性碳吸附異丙醇之機制。由研究結果顯示,異丙醇與活性碳表面為氫鍵作用力之吸附。另外,本研究中亦透過吸附動力模式證實活性碳吸附異丙醇為物理吸附及雙步驟質傳控制。在管柱吸附異丙醇水溶液研究結果顯示,最佳操作參數為異丙醇水溶液初始濃度為1,000 mg/L且體積流率為126.6 mL/min,此條件之下活性碳有相對高的吸附量(30.56 mg/g),亦以此操作參數作為後續蒸氣再生活性碳研究之初始吸附條件。在蒸氣再生活性碳研究中,以蒸汽溫度為140℃且蒸汽流量為3.5 kg/hr之參數操作五次吸脫附迴圈後,再生效率為77.37%。


    Activated carbon has been widely used in the wastewater treatment due to its high porosity and unique surface functionality. Obviously, adsorption of activated carbon is the most important role of wastewater treatment in the optoelectronic industry. As the adsorption process proceeds, the activated carbon becomes saturated with the adsorbate which makes it unacceptable for further utilization and so it has to be replaced by fresh activated carbon or disposed of by incineration or land filling. The regeneration of activated carbon offers clear advantages such as a lower consumption of activated carbon and the possibility of recovering adsorbed products of potential economic value.
    Before the experiment of adsorption of isopropyl alcohol (IPA) aqueous solution in the fixed-bed column, the mechanism of adsorption was determined by conducting the batch adsorption experiment. The interaction of IPA and the surface of activated carbon were through hydrogen bonding and the whole adsorption can be divided into rapid and slow process in this study. In the fixed-bed column adsorption, the optimal operating parameter were that initial concentration with IPA 1,000 mg/L and 126.6 mL/min of volumetric flow rate, which were the operating parameters of steam regeneration of exhausted carbon. In regeneration experiment, there was the regeneration efficiency around 77.37 % after five cycles of adsorption/desorption in the steam temperature of 140 °C and the steam flow rate of 3.5 kg/hr.

    Abstract I 中文摘要 II Acknowledgement III Table of Content IV List of Figure VII List of Table X List of Symbols XII Chapter 1 Introduction 1 1.1 Background 1 1.2 Objectives and Scope 3 Chapter 2 Literature Review 5 2.1 Characteristic of Wastewater in Semiconductor Industry 5 2.1.1 Characteristic of Isopropyl Alcohol 5 2.1.2 Treatment of Isopropyl Alcohol 7 2.2 Adsorption and Desorption of Activated Carbon 8 2.2.1 Characteristic of Activated Carbon 8 2.2.2 Mechanism of Adsorption and Desorption 11 2.2.3 Model Analysis of Adsorption and Desorption 15 2.2.4 Regeneration of Exhausted Activated Carbon 21 2.3 Influences on Activated Carbon Adsorption in Fixed-bed Column 24 2.3.1 Effect of Initial Solution pH 24 2.3.2 Effect of Initial Concentration 25 2.3.3 Effect of Solution Flow Rate 26 2.3.4 Effect of Activated Carbon Bed Height 27 2.4 Steam Regeneration of Exhausted Activated Carbon 29 2.4.1 Principle of Steam Regeneration of Activated Carbon 29 2.4.2 Effect of Steam Temperature 30 2.4.3 Effect of Steam Flow Rate 31 Chapter 3 Materials and Experiments 32 3.1 Chemicals 32 3.2 Experimental Instruments and Apparatus 33 3.2.1 Experimental Instruments 33 3.2.2 Experimental Apparatus 34 3.3 Experimental Procedures 37 3.3.1 Experimental Framework 37 3.3.2 Nomenclature of Activated Carbon 39 3.3.3 Procedures of Adsorption and Desorption 40 3.3.4 Analytic Methods 42 Chapter 4 Results and Discussion 50 4.1 Characteristic Properties of Activated Carbon 50 4.2 Adsorption of IPA on the Activated Carbon in the Batch System 60 4.2.1 Effect of Initial Solution pH 60 4.2.2 Effect of Initial Concentration 63 4.2.3 Effect of Stirring Speed 65 4.2.4 Kinetic and Equilibrium Study of IPA Adsorption 67 4.3 Adsorption of IPA on the Activated Carbon in the Fixed-bed Column 74 4.3.1 Effect of Initial Concentration 74 4.3.2 Effect of Volumetric Flow Rate 77 4.3.3 Model Analysis of Dynamic Adsorption 80 4.4 Steam Regeneration of Exhausted Activated Carbon 89 4.4.1 Effect of Steam Temperature 89 4.4.2 Effect of Steam Flow Rate 91 4.4.3 Effect of Regeneration Cycle 93 Chapter 5 Conclusion and Recommendation 98 5.1 Conclusions 98 5.2 Recommendations 101 Reference 102

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