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研究生: 黃烱秦
Huang, Chiung-Chin
論文名稱: 以鋇系化學過氧沉澱法結合流體化床均質顆粒化技術回收含硼廢水中的硼
Recovery of Boron from Synthetic Wastewater by integrating Barium-based Chemical Oxo-Precipitation with Fluidized-Bed Homogeneous Granulation
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: 2016
畢業學年度: 104
語文別: 中文
論文頁數: 110
中文關鍵詞: 化學過氧沉澱流體化床均質顆粒化流體化床串聯系統晶種(BaB(OH)2(OO)2B(OH)2)
外文關鍵詞: Chemical Oxo-Precipitaiton, Fludized-Bed Homogeneous Granulation, FBRs in series, BaB(OH)2(OO)2B(OH)2
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  • 本研究嘗試將化學過氧沉澱法(COP)結合流體化床均質顆粒化技術(FBHG),將含硼廢水中的硼以低含水率高純度的過硼酸鹽類顆粒型態回收,而非傳統沉澱法所產生高含水率汙泥,同時達到改善水質及資源化含硼廢水中的硼的目標。在單一流體化床之系統,透過pHe、Ba/B、H2O2/B、床高、HRT等變因探討,針對硼濃度600~700 ppm的合成廢水,得以在最佳操作條件下(pHe=9.90、Ba/B=0.84、H2O2/B=1.71、HRT=18 min、靜置床高大於45cm),達到80%的硼總去除率與75%的硼顆粒化率;透過改變進料硼濃度可知單一流體化床除硼系統的最大截面積負荷量為1.6 kg-B/m2·hr;資源化之均質顆粒經由XRD、TEM、Raman交叉比對分析,推測其成分為非結晶相的Ba(B(OH)3OOH)2。流體化床串聯系統則具備處理高濃度含硼廢水(CB,in > 700 ppm)的能力,藉由鋇沉澱劑的分散進料,最終硼總去除率與硼顆粒化率分別可達到80~84%與78%;若於串聯之流體化床填入結晶相沉澱物BaB(OH)2(OO)2B(OH)2作為晶種使用,則可將單一流體化床出流水的殘餘硼溶液有效降至10 ppm以下,系統之硼總去除率(TR)達97.5%,硼顆粒化率(GR)達80%,水質濁度則低於5 NTU。
    關鍵字:化學過氧沉澱、流體化床均質顆粒化、流體化床串聯系統、晶種(BaB(OH)2(OO)2B(OH)2)

    This study investigated the boron recovery from wastewater as moisture content and high purity barium perborate particles by integrating Chemical Oxo-Precipitation with Fluidized-Bed Homogeneous Granulation methods. FBHG-COP could recover boron from wastewater and improve quality of water instead of chemical precipitation producing high moisture content sludge. At research of single FBR system, investigated effect of pHe, molar ratio of Ba/B and H2O2/B, height of column, and HRT for boron wastewater containing 600~700 ppm-B. When operated suitable conditions (pHe=9.90、Ba/B=0.84、H2O2/B=1.71、HRT=18 min、height of column > 45 cm) , the total boron removal ratio (TR) and boron granulation ratio (GR) would get 80% and 75%, respectively. The maximum surface loading of FBHG-COP was 1.6 kg-B/m2·hr by effect of CB,in on boron recovery experiment. The homogeneous particle was Ba(B(OH)3OOH)2 by XRD, TEM, and Raman analysis. The system of FBRs in series could efficiency treat CB,in > 700 ppm wastewater by dividing barium input into half to each reactor. The TR and GR were 80~84% and 78%, respectively. The boron concentration of final effluent water could effectively reduce lower than 10 ppm by adding BaB(OH)2(OO)2B(OH)2 into second FBR. The TR, GR, and turbidity were 97.5%, 80%, and lower than 5 NTU, respectively.

    第一章 緒論 1 1-1 研究緣起 1 1-2 研究目的與內容 2 第二章 文獻回顧 4 2-1 自然界中的硼 4 2-2 硼的應用與污染源 6 2-3 硼的危害及必要性 9 2-3-1 對植物的危害及必要性 9 2-3-2 對動物的危害及必要性 10 2-4 水質標準 11 2-5 水中硼的去除方法 11 2-5-1 薄膜分離法 11 2-5-2 吸附法 13 2-5-3 混凝沉澱法 15 2-5-4 電混凝法 16 2-6 化學過氧沉澱法(Chemical Oxo-Precipitation, COP) 19 2-6-1 硼酸與雙氧水之間的化學反應與過硼酸化學 20 2-6-2 化學過氧沉澱法研究成果 22 2-7 流體化床顆粒化技術 31 2-7-1 流體化床顆粒化(Fluidized-Bed Granulation, FBG) 31 2-7-2 流體化床均質顆粒化(Fluidized-Bed Homogeneous Granulation, FBHG) 34 2-7-3 晶種顆粒化成核理論 36 2-7-4 成核現象 39 第三章 實驗設備、材料與方法 42 3-1 研究架構與流程 42 3-2 實驗設備介紹 45 3-2-1 流體化床反應器 45 3-2-2 批次化學過氧沉澱實驗裝置 46 3-2-3 流體化床串聯系統-處理高濃度含硼廢水 47 3-2-4 流體化床串聯系統-處理殘餘硼濃度 48 3-3 符號及公式定義 49 3-4 實驗藥品 50 3-5 實驗步驟 51 3-5-1 流體化床均質顆粒化除硼最適操作條件探討 51 3-5-2 晶種(BaB(OH)2(OO)2B(OH)2)作為晶種觸批次測試實驗 52 3-5-3 流體化床串聯系統實驗 52 3-6 檢測儀器與分析方法 55 3-6-1 感應耦合電漿原子發射光譜儀 (Inductively Coupled Plasma-Optical Emission Spectrometer; ICP-OES) 55 3-6-2 X光繞射分析儀( X-ray diffraction analyzer, XRD) 56 3-6-3 顯微拉曼光譜儀 (Raman Microscope) 56 3-6-4 掃描式電子顯微鏡 (Scanning Electron Microscope, SEM ) 57 3-6-5 穿透式電子顯微鏡(Transmission Electron Microscopy, TEM) 57 3-6-6 濁度計 (Turbidimeter) 58 第四章 結果與討論 59 4-1 流體化床均質顆粒化除硼最適操作條件 59 4-1-1 H2O2自身降解對FBHG-COP影響 61 4-1-2 顆粒床高對FBHG-COP的影響 63 4-1-3 HRT對FBHG-COP的影響 64 4-1-4 pHe對FBHG-COP的影響 66 4-1-5 莫爾比Ba/B與H2O2/B對FBHG-COP的影響 67 4-1-6 進料硼濃度對FBHG-COP的影響 72 4-1-7 均質顆粒產品鑑定 73 4-2 流體化床串聯系統 80 4-2-1 利用串聯系統處理高濃度含硼廢水 80 4-2-2 批次實驗探討BaB(OH)2(OO)2B(OH)2晶種效應 84 4-2-3 利用串聯系統處理流體化床出流水殘餘的硼 90 第五章 結論與建議 94 5-1 結論 94 5-2 建議 96 參考文獻 97 附錄A過硼酸分布的二元四次方程式求解方法 103 附錄B 過硼酸鋇的流體化床均質顆粒化技術 106

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