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研究生: 林依宣
Lin, I-Hsuan
論文名稱: 以流體化床均質結晶技術自含銅與含鉬廢水中回收Cu3(MoO4)2(OH)2並應用於降解RR195染料
Recovery of Cu3(MoO4)2(OH)2 from Copper- and Molybdenum-Containing Wastewater by Fluidized-Bed Homogeneous Crystallization and Its Application to RR195 Dye Degradation
指導教授: 黃耀輝
Huang, Yao-Hui
學位類別: 碩士
Master
系所名稱: 工學院 - 化學工程學系
Department of Chemical Engineering
論文出版年: 2026
畢業學年度: 114
語文別: 中文
論文頁數: 152
中文關鍵詞: 含銅廢水含鉬廢水流體化床均質結晶Cu3(MoO4)2(OH)2RR195
外文關鍵詞: Copper- and molybdenum-containing wastewater, Fluidized-bed homogeneous crystallization, Cu3(MoO4)2(OH)2, RR195
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  • 隨著電子、光電與金屬表面處理等產業持續發展,含銅與鉬廢水之排放已成為兼具污染防治與資源回收意義的重要議題。為兼顧廢水處理、金屬回收與副產物高值化應用,本研究首先以流體化床均質結晶技術(Fluidized Bed Homogeneous Crystallization, FBHC)處理含銅與鉬廢水,並進一步將回收所得之顆粒應用於UVA/H2O2高級氧化處理程序(Advanced Oxidation Processes, AOPs)以降解RR195模擬染料廢水,藉此建立結合廢水採礦與循環利用之整合技術。
    研究結果顯示,FBHC系統能有效同步去除廢水中的銅與鉬,在適當條件下,兩者的去除率與結晶率皆可達85%至95%以上。經固體產物鑑定分析,顯示回收所得之均質結晶顆粒主要成分為Cu3(MoO4)2(OH)2,證實該技術可將水中的重金屬轉化為具再利用潛力之固體顆粒。
    將此回收之Cu3(MoO4)2(OH)2顆粒直接作為UVA/H2O2系統之催化材料時,發現該廢水副產物具備優異的催化活性,對RR195染料的去除率可高達99%。進一步探討其反應機制,結果表示此系統的降解成效主要來自部分金屬溶出所引發之均相Fenton-like反應與異相催化的協同作用。同時,亦可自自由基抑制試驗的結果推測,超氧/超氧化氫自由基(·O2-/HO2·)可能是反應過程中的關鍵活性氧類之一。
    本研究不僅成功驗證了流體化床均質結晶技術可有效處理含銅與鉬廢水並回收功能性顆粒,更證實了此副產物能作為高級氧化處理程序的有效催化劑,展現重金屬廢水資源化與副產物高值化利用之可行性。

    The discharge of copper- and molybdenum-containing wastewater from industrial processes is a crucial issue for pollution prevention and resource recovery. To simultaneously address wastewater treatment, metal recovery, and high-value by-product application, this study utilized Fluidized Bed Homogeneous Crystallization (FBHC) to treat such wastewater. The recovered granules were subsequently applied to a UVA/H2O2 advanced oxidation process (AOP) to degrade Reactive Red 195 (RR195) dye wastewater, establishing an integrated wastewater mining and recycling technology.
    Results showed the FBHC system effectively and simultaneously removed copper and molybdenum, with removal and crystallization efficiencies reaching 85–95% under appropriate conditions. Characterization confirmed the recovered homogeneous granules were primarily basic copper molybdate Cu3(MoO4)2(OH)2, demonstrating the successful conversion of aqueous heavy metals into solid granules with reuse potential.
    When utilized as catalytic materials in the UVA/H2O2 system, the Cu3(MoO4)2(OH)2 granules exhibited excellent catalytic activity, achieving up to 99% RR195 removal. Mechanistic investigations revealed that this degradation primarily originated from the synergistic effects of heterogeneous catalysis and homogeneous Fenton-like reactions triggered by partial metal leaching. Furthermore, radical scavenging experiments suggested that superoxide/hydroperoxyl radicals (·O2-/HO2·) were among the key reactive oxygen species.
    Overall, this study verifies that FBHC technology can effectively treat heavy metal wastewater and recover functional basic copper molybdate granules. Demonstrating their viability as an AOP catalyst, this research illustrates the dual potential of wastewater resource recovery and the high-value utilization of by-products.

    摘要 i 致謝 vii 目錄 viii 表目錄 xiii 圖目錄 xiv 第一章 緒論 1 1.1 研究緣起 1 1.2 研究目的與內容 5 第二章 文獻回顧 6 2.1 自然界中的鉬與其物理化學特性 6 2.2 鉬的工業應用與廢水來源 7 2.3 鉬之生物必要性、毒性危害與環保法規標準 8 2.4 含鉬廢水處理方法 9 2.4.1 化學沉澱法(Chemical Precipitation) 9 2.4.2 吸附法(Adsorption) 10 2.4.3 離子交換法(Ion Exchange) 11 2.5 自然界中的銅與其物理化學特性 13 2.6 銅的工業應用與污染來源 14 2.7 銅之生物必要性、毒性危害與環保法規標準 15 2.8 工業含銅廢水之處理技術與資源化挑戰 16 2.8.1 化學沉澱法 (Chemical Precipitation) 16 2.8.2 吸附法 (Adsorption) 17 2.8.3 電化學與薄膜分離技術 (Electrochemical and Membrane Separation) 17 2.9 水質化學 19 2.9.1 鉬的物種分佈 19 2.9.2 銅的物種分佈 22 2.9.3 Cu3(MoO4)2(OH)2之溶解度 25 2.10 流體化床結晶技術(Fluidized-Bed Crystallization, FBC) 28 2.10.1 流體化床結晶技術反應器 29 2.10.2 流體化床均質結晶(Fluidized-Bed Homogeneous Crystallization, FBHC)技術 31 2.10.3 結晶、沉澱與過飽和度控制 33 2.10.4 成核、晶體成長與顆粒化機制 34 2.11 RR195反應性染料廢水之特性與處理 35 2.12 含RR195廢水之傳統處理技術及其侷限性 36 2.12.1 生物降解技術與微生物復育 36 2.12.2 物理化學處理與吸附分離技術 36 2.12.3 化學混凝沉澱與薄膜分離技術 37 2.13 高級氧化程序(Advanced Oxidation Process, AOPs) 38 2.13.1 均相芬頓/類芬頓法(Homogeneous Fenton/Fenton-like Process) 38 2.13.2 光芬頓法(Photo-Fenton Process) 39 2.13.3 異相芬頓法(Heterogeneous Fenton Process) 41 第三章 實驗設備、材料與方法 43 3.1 研究架構與流程 43 3.2 實驗裝置介紹 45 3.2.1 凝集試驗機 45 3.2.2 流體化床反應器 45 3.2.3 三相Photo-Fenton反應器 46 3.3 符號及公式定義 48 3.3.1 化學沉澱法之符號及定義公式 48 3.3.2 流體化床均質結晶技術之符號及公式定義 48 3.3.3 高級氧化程序之符號及公式定義 50 3.4 實驗藥品 52 3.5 實驗步驟 53 3.5.1 批次瓶杯試驗 53 3.5.2 流體化床均質結晶技術變因實驗 54 3.5.3 高級氧化程序變因與機制探討實驗 55 3.6 實驗檢測儀器與分析方法 56 3.6.1 感應耦合電漿原子發射光譜儀(Inductively Coupled Plasma-Optical Emission Spectrometer, ICP-OES) 56 3.6.2 X光繞射分析儀(X-ray Diffractometer, XRD) 57 3.6.3 傅立葉轉換式紅外線光譜儀(Fourier-Transform Infrared Spectrometer, FTIR) 58 3.6.4 掃描式電子顯微鏡(Scanning Electron Microscope, SEM) 59 3.6.5 能量散佈光譜儀(Energy Dispersive Spectrometer, EDS) 60 3.6.6 熱重分析儀(Thermogravimetric analysis, TGA) 61 3.6.7 X射線光電子能譜儀(X-ray Photoelectron Spectroscope, XPS) 62 3.6.8 總有機碳分析儀(Total Organic Carbon Analyzer, TOC) 63 3.6.9 紫外光-可見光光譜儀(UV-Visible spectrometer, UV-Vis) 64 第四章 結果與討論 66 4.1 以批次瓶杯試驗(Jar-test)探討最佳除銅與除鉬條件 66 4.1.1 瓶杯試驗之pH值變因探討 66 4.1.2 Cu3(MoO4)2(OH)2熱力學不確定性對模擬結果之影響 70 4.1.3 瓶杯試驗之莫耳比變因探討 73 4.2 以連續式FBHC尋找同時去除銅與鉬之最佳條件 78 4.2.1 FBHC技術回收Cu3(MoO4)2(OH)2之pH值變因探討 80 4.2.2 FBHC技術回收Cu3(MoO4)2(OH)2之莫耳比變因探討 83 4.2.3 FBHC技術回收Cu3(MoO4)2(OH)2之截面負荷變因探討 85 4.2.4 FBHC技術回收Cu3(MoO4)2(OH)2之水力滯留時間變因探討 88 4.2.5 FBHC技術回收Cu3(MoO4)2(OH)2之迴流比變因探討 91 4.2.6 Cu3(MoO4)2(OH)2均質結晶顆粒的分析與鑑定 93 4.2.6.1 Cu3(MoO4)2(OH)2均質結晶顆粒表面形態分析 93 4.2.6.2 Cu3(MoO4)2(OH)2均質結晶顆粒晶相與鍵結分析 94 4.2.6.3 Cu3(MoO4)2(OH)2均質結晶顆粒熱穩定性與元素組成 97 4.2.6.4 Cu3(MoO4)2(OH)2均質結晶顆粒粒徑分析 99 4.3 以高級氧化處理程序(Advanced oxidation process, AOPs)將Cu3(MoO4)2(OH)2均質結晶顆粒應用於去除RR195廢水 100 4.3.1 異相光催化類芬頓實驗pH值變因探討 104 4.3.2 異相光催化類芬頓實驗[H2O2]/[RR195]莫耳比變因探討 108 4.3.3 異相光催化類芬頓實驗Cu3(MoO4)2(OH)2顆粒添加量變因探討 112 4.3.4 異相光催化類芬頓實驗反應機制探討 115 第五章 結論與建議 118 5.1 結論 118 5.2 建議 120 參考文獻 121

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