§ 瀏覽學位論文書目資料
  
系統識別號 U0002-2403201601491900
DOI 10.6846/TKU.2016.00771
論文名稱(中文) 以紫外線結合不同氧化劑程序處理含雙酚A水溶液之光氧化與生物反應研究
論文名稱(英文) Study on the Photooxidation and Biological Reactions of Bisphenol A in Aqueous Solutions by UV/Oxidants Processes
第三語言論文名稱
校院名稱 淡江大學
系所名稱(中文) 水資源及環境工程學系碩士班
系所名稱(英文) Department of Water Resources and Environmental Engineering
外國學位學校名稱
外國學位學院名稱
外國學位研究所名稱
學年度 104
學期 1
出版年 105
研究生(中文) 黃昱閔
研究生(英文) Yu-Min Huang
學號 603480061
學位類別 碩士
語言別 繁體中文
第二語言別
口試日期 2016-01-14
論文頁數 140頁
口試委員 指導教授 - 陳俊成
委員 - 申永順
委員 - 李柏青
關鍵字(中) 高級氧化處理
過氧化氫
過硫酸鹽
雙酚A
WST-1 Assay
細胞毒性
關鍵字(英) Advanced oxidation processes
Hydrogen peroxide
Persulfate
Bisphenol A
HepG2
Cytotoxicity
WST-1 Assay
第三語言關鍵字
學科別分類
中文摘要
高級氧化處理(AOPs)在環境污染物處理上之應用已相當成熟,然如何找出最適合的廢水光催化效率並結合處理後之生物毒性分析,過去僅少數研究者探討。本研究主要針對雙酚A(BPA)經UV/"H" _"2"  "O" _"2" 及UV/SPS處理過後結合生物毒性分析,比較處理前後BPA之降解效率,並探討殘留之污染物及中間產物對生物可能造成的危害。
  實驗結果顯示,在90分鐘的反應後,兩種氧化程序對於BPA之去除皆有顯著效果,然UV/SPS系統之整體去除效率皆優於UV/H2O2系統。光強度於兩種氧化程序皆呈現強度愈強其去除BPA效果愈佳之趨勢,顯示提高UV光穿透水溶液之能力可更快促使氧化劑產生自由基以去除污染物。BPA初始濃度影響著UV光催化氧化劑之能力,高濃度的BPA間接導致氧化劑之催化反應受阻,使BPA之去除效率下降。pH於AOPs降解BPA中扮演著重要角色,研究結果顯示,利用UV/H2O2系統降解BPA在pH為7之環境較為適宜;UV/SPS系統則在pH=3以及pH=11的條件有更加顯著的去除效果。UV/SPS系統礦化BPA之能力即使在低劑量的氧化劑加藥量下仍明顯優於UV/H2O2系統。
  化學反應劑量利用率(RSEs)於兩種氧化程序之各條件操作結果略有不同,顯示氧化劑去除污染物之利用程度亦受各操作因子影響。電能量損耗效益(EE/O)於氧化劑濃度愈高之情況下所需耗能愈低,然過高的氧化劑量對於降低電能損耗並無明顯幫助。由實驗結果所建立之反應速率動力式中觀察得知,UV/H2O2系統對於光強度較具敏感性,UV/SPS系統則較偏向氧化劑。以UV/Thermal/SPS系統降解BPA時,BPA之降解效率隨溫度升高而降低。生物毒性分析方面,UV/H2O2系統降解BPA後仍對HepG2 細胞株肝臟細胞具有一定毒性,顯示BPA於該系統降解過程中產生之中間產物對於細胞仍具影響;UV/SPS系統無論反映前後細胞皆呈現死亡狀態,顯示SPS對細胞具有較大的毒性而失去毒性分析效果。
英文摘要
The decomposition of bisphenol A in aqueous solutions by advanced oxidation processes (UV/H2O2, UV/SPS) under various operational factors (pH, UV light intensity, initial concentration of BPA, and dose of oxidants was studied to evaluate the treatment efficiency. The biotoxicity assay in term of HepG2 cells was applied to the BAP treated wastewaters to be as an indicator of health risk.
  The experimental results revealed that both UV/H2O2 and UV/SPS processes can decompose BPA effectively during90 minutes. Removal rates of BPA by UV/SPS were found to be larger than those by UV/H2O2. The removals of BPA increase with increasing UV light intensity and decreasing with initial concentration of BPA.  The solution pH values affect significantly on the reaction rates of BPA by AOPs, the optimum pH was found to be at neutral conditions by UV/H2O2 compared to those at pH 3 and pH 11 by UV/SPS. The mineralization efficiency of BPA by UV/SPS was larger than those by UV/H2O2 even though at low doses of oxidants.
  Reaction stoichiometric efficiencies (RSEs) were to be determined to evaluate the degree utilization of oxidants and found to be dependent on various operational conditions in the oxidation systems. The EE/O values decreases with increasing the initial concentration of BPA. The chemical kinetic equations for the decomposition of BPA by the two AOPs were established and found that the order of UV light intensity by UV/H2O2 was larger than it by UV/SPS but the order of dose of oxidant by UV/H2O2 was smaller than it by UV/SPS. In the UV/Thermal/SPS system, the treatment efficiency of BPA increases with decreasing temperature. The BPA treated wastewaters by UV/H2O2 and UV/SPS were found to be toxic to HepG2 cells based on the results of biotoxicity assay especially in the UV/SPS system possible due to the residual effect of SPS to kill HepG2 cells.
第三語言摘要
論文目次
目錄 I
圖目錄 V
表目錄 IX
第一章 前言 1
1-1.研究起源 1
1-2.研究目的 3
1-3.研究內容 4
第二章 文獻回顧 5
2-1.環境荷爾蒙 (Endocrine Disrupting Chemicals, EDCs) 5
2-2.高級氧化程序 (Advanced Oxidation Processes, AOPs) 7
2-3.雙酚A (Bisphenol A, BPA) 之物化特性 10
2-4.過氧化氫特性與應用 11
2-5.UV/H2O2 反應機制及相關研究彙整 12
2-6.UV/H2O2 程序操作因子之影響 17
2-6-1.pH之影響 17
2-6-2.H2O2 劑量之影響 18
2-6-3.污染物濃度之影響 19
2-6-4.UV光強度之影響 20
2-7.光化學反應動力模式 22
2-8.過硫酸鹽特性與應用 24
2-9.過硫酸鹽催化之反應機制及相關研究彙整 25
2-10.UV/S2O82- 程序操作因子之影響 32
2-10-1.pH 之影響 32
2-10-2.SPS劑量之影響 33
2-10-3.污染物濃度之影響 34
2-10-4.UV光強度之影響 34
2-10-5.溫度之影響	35
2-11.毒性分析 38
2-11-1.人類肝臟 HepG2 細胞特性 38
2-11-2.以AOPs處理含污染物水溶液並進行毒性分析之相關研究 38
第三章 實驗材料與方法 46
3-1.實驗設備 46
3-2.實驗藥品及藥品配置 47
3-2-1.實驗藥品 47
3-2-2.雙酚A水溶液製備 48
3-2-3.過氧化氫氧化劑儲存溶液製備 48
3-2-4.過硫酸鈉氧化劑儲存溶液製備 48
3-2-5.氧化劑殘餘量分析-碘定量法 48
3-2-6.Dulbecco’s Modified Eagle’s Medium (DMEM) 培養基配製	49
3-2-7.PBS 配製 49
3-3.實驗裝置 51
3-4.細胞株馴養 52
3-5.實驗方法 55
3-5-1.實驗架構 55
3-5-2.化學實驗流程 56
3-5-3.生物實驗流程 56
3-6.分析測定方法 57
3-6-1.光強度分析 57
3-6-2.HPLC分析 57
3-6-3.TOC分析 58
3-6-4.過氧化氫殘餘量測定-碘定量法 58
3-6-5.過硫酸鈉殘餘量測定-碘定量法 59
3-6-6.細胞毒性分析方法 (WST-1) 59
第四章 結果與討論 62
4-1.背景實驗 62
4-1-1.不照光試驗 62
4-1-2.直接光解試驗 63
4-2.以 UV/H2O2 程序降解含雙酚A水溶液之探討 67
4-2-1.光強度效應 67
4-2-2.污染物初始濃度效應 72
4-2-3.氧化劑加藥量效應 76
4-2-4.pH效應 80
4-2-5.污染物礦化情形 85
4-2-6.動力模式 86
4-2-7.生物毒性 88
4-3.以 UV/SPS 程序降解含雙酚A水溶液之探討 91
4-3-1.光強度效應 91
4-3-2.污染物初始濃度效應 96
4-3-3.氧化劑加藥量效應 100
4-3-4.pH效應 104
4-3-5.溫度效應 108
4-3-6.污染物礦化情形 116
4-3-7.動力模式 117
4-3-8.生物毒性 119
4-4.UV/H2O2、UV/SPS 程序處理含雙酚A水溶液之比較 121
4-4-1.光強度效應 122
4-4-2.氧化劑加藥量效應 123
4-4-3.pH效應 125
4-4-4.動力模式 126
第五章 結論與建議	127
5-1. 結論 127
5-2. 建議 131
參考文獻	132


圖目錄
圖2-1 污染物經AOPs處理後之影響評估示意圖 8
圖2-2 藉由UV光催化氧化劑並進行污染物之降解作用 8
圖2-3 由不同高級氧化技術產生氫氧自由基之機制 9
圖2-4 UV/H2O2 去除 EDCs 機制圖 12
圖2-5 不同程序之氧化劑花費與電能量比較圖 35
圖3-1 光反應槽示意圖 51
圖3-2 血球計數盤示意圖 54
圖3-3 整體實驗流程架構 55
圖3-4 雙酚A檢量線 57
圖3-5 Tetrazolium salt WST-1轉變成formazan之示意圖 60
圖3-6 WST-1 加入細胞後之呈色變化 60
圖4-1 BPA = 0.088 mM、molar ratio (BPA/H2O2) = 1:50時BPA之降解情形 62
圖4-2 BPA = 0.088 mM、molar ratio (BPA/SPS) = 1:20時BPA之降解情形 63
圖4-3 不同輸出電壓產生之光強度對照圖 64
圖4-4 不同光強度直接光解BPA之變化圖 65
圖4-5 不同pH直接光解BPA之變化圖 65
圖4-6 雙酚A於不同pH之理論與實際吸光值之比較圖 66
圖4-7 H2O2不同pH之理論與實際吸光值之比較圖 66
圖4-8 UV/H2O2 系統中不同光強度降解BPA之變化圖 68
圖4-9 UV/H2O2系統中不同光強度降解BPA之反應動力常數變化圖 68
圖4-10 UV/H2O2 系統中 H2O2 於不同光強度之殘餘量變化圖 70
圖4-11 UV/H2O2 系統中不同光強度之利用率變化圖 70
圖4-12 UV/H2O2 系統中不同光強度所需之電耗能變化圖 71
圖4-13 UV/H2O2 系統中實際投入水體之不同光強度所需電耗能變化圖 72
圖4-14 UV/H2O2 系統中不同BPA初始濃度經降解之變化圖 73
圖4-15 UV/H2O2 系統中不同BPA初始濃度經降解之反應動力常數變化圖 74
圖4-16 UV/H2O2 系統中 H2O2 於不同BPA初始濃度之殘餘量變化圖 75
圖4-17 UV/H2O2 系統中不同BPA初始濃度之利用率變化圖 75
圖4-18 UV/H2O2系統中不同 H2O2 加藥量去除BPA之變化圖 77
圖4-19 UV/H2O2系統中不同 H2O2 加藥量去除 BPA 之反應動力常數變化圖 77
圖4-20 UV/H2O2 系統中 H2O2 於不同氧化劑加藥量之殘餘量變化圖 78
圖4-21 UV/H2O2 系統中不同氧化劑加藥量之利用率變化圖 79
圖4-22 UV/H2O2 系統中不同氧化劑加藥量所需之電耗能變化圖 79
圖4-23 UV/H2O2系統中不同pH去除BPA之變化圖 82
圖4-24 UV/H2O2系統中不同pH去除BPA之反應動力變化圖 82
圖4-25 UV/H2O2 系統中 H2O2 於不同 pH 之殘餘量變化圖 83
圖4-26 UV/H2O2 系統中不同pH之利用率變化圖 84
圖4-27 UV/H2O2 系統中不同pH所需之電耗能變化圖 84
圖4-28 UV/H2O2 系統中不同加藥量於90分鐘後 TOC 之降解情形 86
圖4-29 UV/ H2O2 不同加藥量與降解 BPA 之動力常數線性預測圖 87
圖4-30 UV/ H2O2 不同光強度與降解 BPA 之反應動力常數線性預測圖 87
圖4-31 HepG2 於各條件之細胞生長情形 (4x) 88
圖4-32 HepG2 於各條件之生長情形 (10x) 89
圖4-33 UV/H2O2 系統中BPA經處理前後之細胞毒性影響 90
圖4-34 UV/SPS 系統中不同光強度去除BPA之變化圖 92
圖4-35 UV/SPS 系統中不同光強度去除BPA之反應動力常數變化圖 92
圖4-36 UV/SPS 系統中 SPS 於不同光強度之殘餘量變化圖 94
圖4-37 UV/SPS 系統中不同光強度之利用率變化圖 95
圖4-38 UV/SPS 系統中不同光強度所需之電耗能變化圖 95
圖4-39 UV/SPS 系統中實際投入水體之不同光強度所需電耗能變化圖 96
圖4-40 UV/SPS 系統中去除不同BPA初始濃度經降解之變化圖 97
圖4-41 UV/SPS 系統中去除不同 BPA 初始濃度之反應動力變化圖 98
圖4-42 UV/SPS 系統中 SPS 於不同BPA初始濃度之殘餘量變化圖 99
圖4-43 UV/SPS 系統中不同BPA初始濃度之利用率變化圖 99
圖4-44 UV/SPS 系統中不同SPS加藥量去除BPA之變化圖 101
圖4-45 UV/SPS 系統中不同SPS加藥量去除BPA之反應動力常數變化圖 101
圖4-46 UV/SPS 系統中 SPS 於不同BPA初始濃度之殘餘量變化圖 103
圖4-47 UV/SPS 系統中不同氧化劑加藥量之利用率變化圖 103
圖4-48 UV/SPS 系統中不同氧化劑加藥量所需之電耗能變化圖 104
圖4-49 UV/SPS 系統中不同 pH 去除 BPA 之變化圖 105
圖4-50 UV/SPS 系統中不同 pH 去除 BPA 之反應動力變化圖 105
圖4-51 UV/SPS 系統中 SPS 於不同pH之殘餘量變化圖 106
圖4-52 UV/SPS 系統中不同 pH 之利用率變化圖 107
圖4-53 UV/SPS 系統中不同 pH 所需之電耗能變化圖 107
圖4-54 Thermal/SPS 系統中不同溫度去除 BPA 之變化圖 109
圖4-55 UV/Thermal/SPS 系統中不同溫度去除BPA之變化圖	109
圖4-56 UV/Thermal/SPS 系統反應10分鐘後 BPA 與中間產物之分佈情形 110
圖4-57 UV/Thermal/SPS 系統反應20分鐘後 BPA 與中間產物之分佈情形 110
圖4-58 UV/Thermal/SPS 系統反應40分鐘後 BPA 與中間產物之分佈情形 111
圖4-59 BPA 經OH‧降解之機制圖 111
圖4-60 BPA 經 SO4-‧降解之機制圖 112
圖4-61 UV/Thermal/SPS 系統中不同溫度去除 BPA 之反應動力變化圖 113
圖4-62 UV/Thermal/SPS系統中 SPS 於不同溫度之殘餘量變化圖 114
圖4-63 UV/Thermal/SPS 系統中不同溫度之利用率變化圖 114
圖4-64 於未照光及照光之條件下升溫催化 SPS 降解 BPA 之 Arrhenius 線性圖 115
圖4-65 UV/SPS 系統中不同加藥量於90分鐘後TOC之降解情形 116
圖4-66 UV/ SPS 不同加藥量與降解 BPA 之動力常數線性預測圖 118
圖4-67 UV/SPS 不同光強度與降解 BPA 之反應動力常數線性預測圖 118
圖4-68 UV/SPS 系統中BPA於 pH 3經處理前後之細胞毒性影響 119
圖4-69 UV/SPS 系統中BPA於 pH 5經處理前後之細胞毒性影響 120
圖4-70 UV/SPS 系統中BPA於 pH 11經處理前後之細胞毒性影響 120
圖4-71 OH‧與 SO4-‧降解目標有機物之機制圖 121
圖4-72 兩種氧化劑於不同光強度之降解 BPA 反應動力常數比較圖 122
圖4-73 相同莫耳濃度之氧化劑於不同光強度之降解 BPA 反應動力常數比較圖 123
圖4-74 兩種氧化劑於不同氧化劑劑量之降解 BPA 反應動力常數比較圖 124
圖4-75 相同莫耳濃度之氧化劑於不同氧化劑劑量之降解 BPA 反應動力常數比較圖 124
圖4-76 兩種氧化劑於pH之降解 BPA 反應動力常數比較圖 125
圖4-77 相同莫耳濃度之氧化劑於pH之降解 BPA 反應動力常數比較圖 126


表目錄
表2-1 常見的氧化劑標準還原電位 7
表2-2 雙酚A之物化特性 10
表2-3 過氧化氫之物化特性 11
表2-4 以 UV/H2O2 處理 EDCs、藥物等之相關研究 13
表2-5 過硫酸鹽之物化特性 24
表2-6 有機物存在UV/S2O82-時之反應機制 27
表2-7 以UV/SPS 及 Themal/SPS處理含EDCs, 抗生素之相關研究 29
表2-8 以 AOPs 處理含污染物水溶液並進行毒性分析之文獻彙整 40
表2-9 AOPs 處理真實水體所扮演的角色以及相對應之生物分析之角色 42
表2-10 飲用水經過AOPs處理後之毒性/雌激素活性測試與結論 43
表3-1 本研究所需各項實驗設備之來源與目的 46
表3-2 實驗藥品 47
表3-3 PBS配方表 50
表3-4 使用HPLC於雙酚A水溶液之操作條件 58
表4-1 不同光強度之貢獻率比較 69
表4-2 UV/H2O2 系統中不同BPA初始濃度經降解之貢獻率比較 74
表4-3 UV/H2O2 系統中不同 H2O2 加藥量之貢獻率比較 78
表4-4 UV/H2O2系統中不同pH去除BPA之貢獻率比較 83
表4-5 UV/SPS 系統中不同光強度去除BPA之貢獻率比較 93
表4-6 UV/SPS 系統中去除不同 BPA 初始濃度之貢獻率比較 98
表4-7 UV/SPS 系統中不同SPS加藥量去除BPA之貢獻率比較 102
表4-8 UV/SPS 系統中不同 pH 去除 BPA 之貢獻率比較 106
表4-9 UV/Thermal/SPS 及Thermal/SPS系統中去除 BPA 之貢獻率比較 113
參考文獻
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