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研究生:蔡嘉仁
研究生(外文):Chia-jen Tsai
論文名稱:廢棄活性白土對水溶液中重金屬之吸附特性研究
論文名稱(外文):Adsorption Characteristic of Heavy Metals Onto Spent Activacted Clay
指導教授:翁誌煌翁誌煌引用關係
指導教授(外文):Chih-Huang Weng
學位類別:碩士
校院名稱:義守大學
系所名稱:材料科學與工程學系
學門:工程學門
學類:材料工程學類
論文種類:學術論文
論文出版年:2005
畢業學年度:93
語文別:中文
中文關鍵詞:活性白土動力吸附平衡吸附
外文關鍵詞:Active ClayCopperNickelZincLeadCadmiumPower AdsorptionBalance Adsorption
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本研究探討工廠廢棄活性白土吸附水溶液重金屬之特性,以銅、鎳、鋅、鉛、鎘五種重金屬離子作為吸附對象,研究探討相關操作條件對其吸附特性的影響,包括:溶液pH值、離子強度、重金屬濃度、溫度等因子,以了解廢棄活性白土對五種重金屬離子吸附行為之影響。
廢棄活性白土經由咖啡機沸水沖洗,其吸附效果顯著,結果發現,加熱處理過之廢棄活性白土,其吸附效果雖低於活性白土(Activated Clay),卻相對明顯高於廢棄活性白土,為一吸附性質頗佳之材料。
咖啡機清洗廢棄活性白土(SAC)對水溶液中重金屬離子去除之研究結果顯示,經由動力及平衡吸附試驗,在pH值增高的情況下,重金屬離子被吸附有增加之趨勢。而在低離子濃度及高反應溫度(50℃)下,對吸附重金屬離子,會呈現較高的去除效率。且離子強度增加,咖啡機處理廢棄活性白土吸附重金屬離子則有減少趨勢。結果顯示試驗條件如各重金屬濃度的改變、pH值的變化、溫度的高低、離子強度的不同,對其去除率皆會有不同之影響。
This thesis was forcus on studying adsorption characteristic of heavy metals onto spent activated clay(SPAC). Five metals,Cu, Ni, Zn,Pb,Cd were used as absorbate. Parameters that may be affected the adsorption including, solution pH, ionic strength, metal concentration, and temperature were conducted.
Experimental results showed that the SPAC treated by coffee machine. Exhibited in a higher adsorption capacities than that of the SPAC without treated. Results also showed both increasing pH and temperature could increase the adsorption. However, as experimental condition was controlled at low ionic strength, the adsorption capacity was decreased according. The result,also demonstrated as changing the testing conditions including, heavy metals concentration, the pH, the temperature, the ion intensity , all can have the different influence to its removing rate.
摘要…………………………………………Ι
英文摘要……………………………………………………Ⅱ
目錄……………………………………………………Ⅲ
圖目錄……………………………………………………Ⅶ
表目錄……………………………………………………ⅩⅣ
第一章 緒論 ……………………………………………………1
1-1 前言……………………………………………………………………1
1-2 研究目的與內容………………………………………………………3
第二章 文獻回顧……………………………………………………4
2-1 活性白土資源化技術…………………………………………………4
2-2 吸附原理及理論………………………………………………………6
2-3 等溫吸附模式…………………………………………………………7
2-4 吸附特性之主要影響因子……………………………………………11
第三章 研究材料與方法……………………………………………………12
3-1 研究流程………………………………………………………………12
3-2 研究設備與儀器………………………………………………………13
3-3 實驗器皿之清潔………………………………………………………14
3-4 研究材料及藥品………………………………………………………14
3-5 研究方法………………………………………………………………18
3-6 實驗控制條件…………………………………………………………22
3-7 分析方法………………………………………………………………25
3-8 活性白土與未處理、已處理廢棄活性白土之吸附重金屬動力實驗
綜合比較………………………………………………………………30
第四章 結果與討論……………………………………………………32
4-1 Cu動力吸附實驗……………………………………………………32
4-1-1不同Cu初始濃度下SAC吸附Cu之影響……………………32
4-1-2不同離子強度下SAC吸附Cu之影響…………………………34
4-1-3不同pH值下SAC吸附Cu之影響……………………………37
4-1-4不同溫度下對SAC吸附Cu之影響……………………………39
4-1-5不同吸附劑下吸附Cu之影響……………………………………41
4-2 Ni動力吸附實驗……………………………………………………44
4-2-1不同Ni初始濃度下SAC吸附Ni之影響………………………44
4-2-2不同離子強度下SAC吸附Ni之影響…………………………46
4-2-3不同pH值下SAC吸附Ni之影響………………………………48
4-2-4不同溫度下SAC吸附Ni之影響………………………………50
4-2-5不同吸附劑下SAC吸附Ni之影響……………………………52
4-3 Zn動力吸附實驗……………………………………………………54
4-3-1不同Zn初始濃度下SAC吸附Zn之影響………………………54
4-3-2不同離子強度下SAC吸附Zn之影響…………………………56
4-3-3不同pH值下SAC吸附Zn之影響………………………………58
4-3-4不同溫度下SAC吸附Zn之影響………………………………60
4-3-5不同吸附劑對SAC吸附Zn之影響……………………………62
4-4 Pb動力吸附實驗……………………………………………………64
4-4-1 不同Pb初始濃度下SAC吸附Pb之影響………………………64
4-4-2 不同離子強度下SAC吸附Pb之影響…………………………66
4-4-3 不同條件pH值下SAC吸附Pb之影響…………………………68
4-4-4不同溫度下SAC吸附Pb之影響…………………………………69
4-4-5不同吸附劑下SAC吸附Pb之影響………………………………71
4-5 Cd動力吸附實驗…………………………………………………73
4-5-1不同Cd初始濃度下SAC吸附Cd之影響………………………73
4-5-2不同離子強度下SAC吸附Cd之影響……………………………75
4-5-3不同pH值下SAC吸附Cd之影響………………………………77
4-5-4不同溫度下SAC吸附Cd之影響…………………………………79
4-5-5不同吸附劑下SAC吸附Cd之影響………………………………81
4-6 不同重金屬動力實驗影響因子綜合比較……………………………83
4-7 Cu平衡吸附實驗……………………………………………………85
4-7-1 pH值對SAC吸附Cu之影響……………………………………85
4-7-2離子強度對Cu平衡吸附線之影響………………………………86
4-7-3 pH值對Cu吸附等溫線之影響……………………………………88
4-7-4溫度對Cu吸附等溫線之影響……………………………………90
4-7-5各種材料對Cu去除之概況………………………………………93
4-8 Ni平衡吸附…………………………………………………………95
4-8-1 pH值對SAC吸附Ni之影響………………………………………95
4-8-2離子強度對Ni平衡吸附線之影響………………………………96
4-8-3 pH值對Ni吸附等溫線之影響……………………………………98
4-8-4溫度對Ni吸附等溫線之影響……………………………………99
4-8-5各種材質對Ni去除之概況………………………………………101
4-9 Zn恆溫平衡吸附實驗……………………………………………104
4-9-1 pH值對SAC吸附Zn之影響……………………………………104.
4-9-2離子強度對Zn平衡吸附線之影響………………………………105
4-9-3 pH值對Zn吸附等溫線之影響…………………………………107
4-9-4溫度對Zn吸附等溫線之影響……………………………………108
4-9-5各種材質對Zn去除之概況………………………………………111
4-10 Pb恆溫平衡吸附實驗……………………………………………112
4-10-1 pH值對SAC吸附Pb之影響…………………………………112
4-10-2離子強度對Pb平衡吸附線之影響……………………………113
4-10-3 pH值對Pb吸附等溫線之影響…………………………………115
4-10-4溫度對Pb吸附等溫線之影響…………………………………116
4-10-5各種材料對Pb去除之概況……………………………………119
4-11 Cd恆溫平衡吸附實驗…………………………………………120
4-11-1不同pH值下SAC吸附Cd之百分比影響……………………120
4-11-2離子強度吸附Cd平衡吸附線之影響…………………………121
4-11-3 pH值對Cd吸附等溫線之影響………………………………123
4-11-4溫度對Cd吸附等溫線之影響…………………………………124
4-11-5各種材料對Cd去除之概況……………………………………126
4-12 不同重金屬平衡實驗影響因子綜合比較………………………128
第五章 結論與建議…………………………………………………………130
5-1 結論……………………………………………………………130
5-2 建議……………………………………………………………132
參考文獻……………………………………………………………………133
圖目錄
Fig2-1-1 活性白土……………………………………………………………5
Fig2-3-1 吸附等溫曲線分類………………………………………………10
Fig3-1-1 咖啡機清洗廢棄活性白土對重金屬吸附試驗架構圖 …………15
Fig3-4-1 活性白土 …………………………………………………………15
Fig3-4-2 廢棄活性白土 ……………………………………………………15
Fig3-4-3 咖啡機熱處理廢棄活性白土 ……………………………………15
Fig3-4-4 活性白土SEM影像 x600 ………………………………………16
Fig3-4-5 廢棄活性白土SEM影像 x200 ……………………………………16
Fig3-4-6 廢棄活性白土SEM影像 x500 ……………………………………16
Fig3-5-1 Comparison different adsorbets for SAC adsorption kinetics………19
Fig3-7-1 Relationship between Cu prepares and measwerd from AA………26
Fig3-7-2 Relationship between Ni prepares and measwerd from AA………27
Fig3-7-3 Relationship between Zn prepares and measwerd from AA………28
Fig3-7-4 Relationship between Pb prepares and measwerd from AA………29
Fig3-7-5 Relationship between Cd prepares and measwerd from AA………30
Fig3-8-1 Comparison different adsorbets for Cu adsorption kinetics;solid lines represent best fit of modified Freundlich equation………………31
Fig4-1-1 Effect of initial Cu (Ⅱ) concentration on adsorption kinetics; solid lines represent best fit of modified Freundlich equations…………33
Fig4-1-2 Realtionship between initial Cu concentration and rate constant k , Data was obtained from Table 4-1-1………………………………34
Fig4-1-3 Effect of ionic strength on adsorption kinetics;solid lines represent best fit of modified Freundlich.equation.………………………35
Fig4-1-4 Realtionship between ionic strength concentration and rate constant k , Data was obtained from Table 4-1-2………………………………36
Fig4-1-5 Effect of pH on adsorption kinetics; solid lines represent best fit of modified Freundlich. Equation……………………………………38
Fig4-1-6 Effect of temperature on adsorption kinetics; solid lines represent best fit of modified Freundlich.equation.………………………………40
Fig4-1-7 Piot for determination of acfivation energy E for the kinetic adsorption of Cu(Ⅱ) onto SAC………………………………………………41
Fig4-1-8 Comparison different adsorbets for Cu adsorption kinetics; solid lines represent best fit of modified Freundlich. equation………………42
Fig4-2-1 Effect of initial Ni (Ⅱ) concentration on adsorption kinetics;solid lines represent best fit of modified Freundlich equations…………………44
Fig4-2-2 Realtionship between initial Ni concentration and rate constant k , Data was obtained from Table 4-2-1……………………………………45
Fig4-2-3 Effect of ionic strength on adsorption kinetics; solid lines represent best fit of modified Freundlich equation………………………………47
Fig4-2-4 Realtionship between ionic strength concentration and rate constant k , Data was obtained from Table 2…………………………………48
Fig4-2-5 Effect of pH on adsorption kinetics; solid lines represent best fit of modified Freundlich equation…………………………………49
Fig4-2-6 Effect of temperature on adsorption kinetics; solid lines represent best fit of modified Freundlich. equation……………………………51
Fig4-2-7 Piot for determination of acfivation energy E for the kinetic adsorption of Ni(Ⅱ) onto SAC……………………………………………52
Fig4-2-8 Comparison different adsorbets for Ni adsorption kinetics; solid lines represent best fit of modified Freundlich. equation……………53
Fig4-3-1 Effect of initial Zn (Ⅱ) concentration on adsorption kinetics;solid lines represent best fit of modified Freundlich equations……………54
Fig4-3-2 Realtionship between initial Zn concentration and rate constant k , Data was obtained from Table 4-3-1………………………………55
Fig4-3-3 Effect of ionic strength on adsorption kinetics; solid lines represent best fit of modified Freundlich equation…………………………57
Fig4-3-4 Realtionship between ionic strength concentration and rate constant k , Data was obtained from Table 4-3-2…………………………58
Fig4-3-5 Effect of pH on adsorption kinetics; solid lines represent best fit of modified Freundlich. Equation………………………………59
Fig4-3-6 Effect of temperature on adsorption kinetics; solid lines represent best fit of modified Freundlich. equation…………………………61
Fig4-3-7 Piot for determination of acfivation energy E for the kinetic adsorption of Zn(Ⅱ) onto SAC………………………………………62
Fig4-3-8 Comparison different adsorbets for Zn adsorption kinetics; solid lines represent best fit of modified Freundlich. equation…………………63
Fig4-4-1 Effect of initial Pb (Ⅱ) concentration on adsorption kinetics;solid lines represent best fit of modified Freundlich equations…………………64
Fig4-4-2 Realtionship between initial Pb concentration and rate constant k , Data was obtained from Table 4-4-1…………………………………65
Fig4-4-3 Effect of ionic strength on adsorption kinetics; solid lines represent best fit of modified Freundlich equation………………………………66
Fig4-4-4 Realtionship between ionic strength concentration and rate constant k , Data was obtained from Table 4-4-2………………………………67
Fig4-4-5 Effect of pH on adsorption kinetics; solid lines represent best fit of modified Freundlich. equation……………………………………68
Fig4-4-6 Effect of temperature on adsorption kinetics; solid lines represent best fit of modified Freundlich. equation………………………………70
Fig4-4-7 Piot for determination of acfivation energy E for the kinetic adsorption of Pb (Ⅱ) onto SAC……………………………………………71
Fig4-4-8 Comparison different adsorbets for Pb adsorption kinetics; solid lines represent best fit of modified Freundlich. equation………………72
Fig4-5-1 Effect of initial Cd (Ⅱ) concentration on adsorption kinetics;solid lines represent best fit of modified Freundlich equations…………………73
Fig4-5-2 Realtionship between initial Cd concentration and rate constant k , Data was obtained from Table 4-5-1………………………………74
Fig4-5-3 Effect of ionic strength on adsorption kinetics; solid lines represent best fit of modified Freundlich equation………………………………75
Fig4-5-4 Realtionship between ionic strength concentration and rate constant k , Data was obtained from Table 4-5-2………………………………76
Fig4-5-5 Effect of pH on adsorption kinetics; solid lines represent best fit of modified Freundlich. Equation……………………………………78
Fig4-5-6 Effect of temperature on adsorption kinetics; solid lines represent best fit of modified Freundlich. Equation………………………………80
Fig4-5-7 Piot for determination of acfivation energy E for the kinetic adsorption of Cd (Ⅱ) onto SAC……………………………………………81
Fig4-5-8 Comparison different adsorbets for Cd adsorption kinetics; solid lines represent best fit of modified Freundlich. equation…………………82
Fig4-6-1 Effect of initial Metal concentration on adsorption kinetics; solid lines represent best fit of modified Freundlich equations…………………83
Fig4-7-1 Surface Complex formation model. Experimental conditions………85
Fig4-7-2 Effect of ionic strength on the isotherm for Cu adsorption onto SAC ………………………………………………………………87
Fig4-7-3 Relationship between the equilibrium adsorption constants, K, and the first layer adsorption density, Qm, on the thickness of the electrical double layer, 1/κ…………………………………………………88
Fig4-7-4 Effect of pH on the isotherm for Cu adsorption onto SAC (Spent Activated Clay)…………………………………………………89
Fig 4-7-5 Effect of temperature on the isotherm for Cu adsorption onto SAC (Spent Activated Clay) ……………………………………………91
Fig4-7-6 Relationship between ln K and1/T. ………………………………92
Fig4-8-1 Surface Complex formation model. Experimental conditions………95
Fig4-8-2 Effect of ionic strength on the isotherm for Ni adsorption onto SAC ………………………………………………………96
Fig4-8-3 Relationship between the equilibrium adsorption constants, K, and the first layer adsorption density, Qm, on the thickness of the electrical double layer, 1/κ…………………………………………………97
Fig4-8-4 Effect of pH on the isotherm for Ni adsorption onto SAC…………98
Fig4-8-5 Effect of temperature on the isotherm for Ni adsorption onto SAC……………………………………………………………100
Fig4-8-6 Relationship between ln K and1/T………………………………101
Fig4-9-1 Surface Complex formation model.………………………………104
Fig4-9-2 Effect of ionic strength on the isotherm for Ni adsorption onto SAC……………………………………………………………105
Fig4-9-3 Relationship between the equilibrium adsorption constants, K, and the first layer adsorption density, Qm, on the thickness of the electrical double layer, 1/κ…………………………………………………106
Fig4-9-4 Effect of pH on the isotherm for Zn adsorption onto SAC…………107
Fig4-9-5 Effect of temperature on the isotherm for Zn adsorption onto SAC……………………………………………………………109
Fig4-9-6 Relationship between ln K and1/T………………………………110
Fig4-10-1 Surface Complex formation model.………………………………112
Fig4-10-2 Effect of ionic strength on the isotherm for Pb adsorption onto SAC…………………………………………………………113
Fig4-10-3 Relationship between the equilibrium adsorption constants, K, and the first layer adsorption density, Qm, on the thickness of the electrical double layer, 1/κ………………………………………………114
Fig4-10-4 Effect of pH on the isotherm for Pb adsorption onto SAC……………………………………………………………115
Fig4-10-5 Effect of temperature on the isotherm for Pb adsorption onto SAC…………………………………………………………117
Fig4-10-6 Relationship between ln K and1/T………………………………118
Fig4-11-1 Surface Complex formation model………………………………120
Fig4-11-2 Effect of ionic strength on the isotherm for Cd adsorption onto SAC …………………………………………………………121
Fig4-11-3 Relationship between the equilibrium adsorption constants, K, and the first layer adsorption density, Qm, on the thickness of the electrical double layer, 1/κ………………………………………………122
Fig4-11-4 Effect of pH on the isotherm for Cd adsorption onto SAC………123
Fig4-11-5 Effect of temperature on the isotherm for Cd adsorption onto SAC……………………………………………………………125
Fig4-11-6 Relationship between ln K and1/T………………………………126
Fig4-12-1 Effect of temperature on the isotherm for Cu 、Ni 、Zn、 Pb、 Cd adsorption onto SAC. ………………………………………128
表目錄
Table2-3-1 處理對策……………………………………………………………5
Table2-3-1 物理吸附與化學吸附之比較………………………………………7
Table3-4-1 活性白土特性分析…………………………………………………17
Table3-4-2 活性白土的性質……………………………………………………17
Table3-5-1 各種白土處理情形之比表面積及平均孔徑………………………20
Table3-6-1 動力實驗控制條件(Cu、Ni、Zn、Pb、Cd)………………… 24
Table3-6-2 平衡吸附條件(Cu、Ni、Zn、Pb、Cd)……………………… 25
Table3-8-1 Modified Freundlich Constants for adsorption of Cu onto SAC … 31
Table4-1-1 Modified Freundlich Constants for adsorption of Cu onto SAC…33
Table4-1-2 Modified Freundlich Constants for adsorption of Cu onto SAC…36
Table4-1-3 Modified Freundlich Constants for adsorption of Cu onto SAC…38
Table4-1-4 Modified Freundlich Constants for adsorption of Cu onto SAC…40
Table4-1-5 Modified Freundlich Constants for adsorption of Cu onto SAC…43
Table4-1-6 各種吸附劑之比表面積及平均孔徑……………………………43
Table4-2-1 Modified Freundlich Constants for adsorption of Ni onto SAC…45
Table4-2-2 Modified Freundlich Constants for adsorption of Ni onto SAC…47
Table4-2-3 Modified Freundlich Constants for adsorption of Ni onto SAC…49
Table4-2-4 Modified Freundlich Constants for adsorption of Cu onto SAC…51
Table4-2-5 Modified Freundlich Constants for adsorption of Ni onto SAC…53
Table4-3-1 Modified Freundlich Constants for adsorption of Zn onto SAC…54
Table4-3-2 Modified Freundlich Constants for adsorption of Zn onto SAC…55
Table4-3-3 Modified Freundlich Constants for adsorption of Znonto SAC…59
Table4-3-4 Modified Freundlich Constants for adsorption of Zn onto SAC…61
Table4-3-5 Modified Freundlich Constants for adsorption of Zn onto SAC…63
Table4-4-1 Modified Freundlich Constants for adsorption of Pb onto SAC…65
Table4-4-2 Modified Freundlich Constants for adsorption of Pb onto SAC…67
Table4-4-3 Modified Freundlich Constants for adsorption of Pb onto SAC…69
Table4-4-4 Modified Freundlich Constants for adsorption of Pb onto SAC…70
Table4-4-5 Modified Freundlich Constants for adsorption of Pb onto SAC…72
Table4-5-1 Modified Freundlich Constants for adsorption of Pb onto SAC…74
Table4-5-2 Modified Freundlich Constants for adsorption of Cd onto SAC…76
Table4-5-3 Modified Freundlich Constants for adsorption of Cd onto SAC…78
Table4-5-4 Modified Freundlich Constants for adsorption of Cd onto SAC…80
Table4-5-5 Modified Freundlich Constants for adsorption of Cd onto SAC…82
Table4-6-1 Comparison of rate constant(k)and(m)for 5metals…………84
Table4-7-1 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption .…………………………………87
Table4-7-2 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.…………………………………89
Table4-7-3 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption…………………………………92
Table4-7-4 Thermodynamic parameters for the adsorption of Cu onto SAC…92
Table4-7-5 Adsorption Capacity of Cu(II) by Various Adsorbents…………94
Table4-8-1 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption…………………………………97
Table4-8-2 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.…………………………………99
Table4-8-3 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………100
Table4-8-4 Thermodynamic parameters for the adsorption of Ni onto SAC…101
Table4-8-5 Adsorption Capacity of Ni(II) by Various Adsorbents…………103
Table4-9-1 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption…………………………………106
Table4-9-2 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………108
Table4-9-3 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………110
Table4-9-4 Thermodynamic parameters for the adsorption of Zn ontoSAC…110
Table4-9-5 Adsorption Capacity of Zn(II) by Various Adsorbents…………111
Table4-10-1 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………114
Table4-10-2 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………116
Table4-10-3 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………117
Table4-10-4 Thermodynamic parameters for the adsorption of Pb onto SAC …………………………………………………………118
Table4-10-5 Adsorption Capacity of Pb(II) by Various Adsorbents…………119
Table4-11-1 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………122
Table4-11-2 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption.………………………………124
Table4-11-3 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption………………………………125
Table4-11-4 Thermodynamic parameters for the adsorption of Cd onto SAC …………………………………………………………126
Table4-11-5 Adsorption Capacity of Cd (II) by Various Adsorbents………127
Table4-12-1 Equilibrium adsorption constants and specific surface area as determined by SAC adsorption. ………………………………129
Table4-12-2 Thermodynamic parameters for the adsorption of Cu 、Ni 、Zn、 Pb、 Cd onto SAC.………………………………………… 129
參考文獻
[1]. Ayala, J., Blanco, F., Garcia, P., Rodriguez, P. and Sancho, J.,
“Asturian Fly Ash as a Heavy Metals Removal Material”, Fuel and
Energy Abstracts, vol. 77, no. 11, pp. 1147-1154, 1998.
[2]. Ali, A. A-H. A., and El-Bishtawi, R. “Removal of Lead and Nickelions
Using Zeolite”, Journal Chemistry Technology and Biotechnology,
vol. 69, pp. 27-34, 1997.
[3]. Barrow, N. J., “A Brief Discussion on the Effect of Temperature on the
Reaction of Inorganic Ions with Soil”, Journal of Soil Science, vol. 43,
no.1, pp. 37-45, 1992.
[4]. Boekhold, A. E. and Temminghoff, E. J. M., “Influence of E1ectrol Yte
Composition and pH on Cadmium Sorption by an Acid Sandy Soil”,
Journal of Soil Science, vol. 44, no. 1, pp.85-96, 1993.
[5]. Corapcioglu, M. O. and Huang, C. P., “The Adsorption of Heavymetals
onto Hydrous Activated Carbon”, Water Research, vol. 21, no. 9, pp
1031-1044, 1987.
[6]. Corapcioglu, M. O. and Huang., C. P., “The Surface Acidity and
Characterization of Some Commercial Activated Carbons”, Carbon., vol.
25, no.4, pp.569-578, 1987.
[7]. Daido, M., “A Recovery and Reuse System for Fatty Oils from By-product and Waste Materials of Vegetable Fatty Oil Production”, Conservation & Recycling, vol. 4, no.10, pp.273-278, 1987.
[8]. Degodo, A. L., Perez, C. and Copez, F. A., “Sorption of Heavy Metals on Blast Furnace Sludge”, Journal Chemical Technology and Biotechnology, vol. 32, pp.1989-1996, 1998.
[9]. Dimitrova, S. V. and Mehanjiev, D. R., “Lead Removal from Aqueous
Solutions by Granulated Blast-Furnace Slag”, Water Research, vol. 32,
no. 11, pp.3289-3292, 1998.
[10]. Elliott, H. A. and Huang, C. P., “Factors Affecting the Adsorption of Complexed Heavy Metals on Hydrous Al2O3”, Water Science and Technology, vol. 17, no. 4, pp.1017-1028, 1984.
[11]. Ferro-Gracia, M. A., Utrilla, R. J. and Toledo, B. I., “Adsorption of Zinc, Cadmium and Copper on Activated Carbons Obtained from Agricultural by-Products”, Carbon. vol. 26, pp.263-273, 1988.
[12]. Filho, N. L. D., Gushiken, Y., Polito, W. L. and Moreiza, J. C., “Sorption and Preconcentrations of Metalions in Ethanolsolutions With Silica Gel Modified With Benzinmidazole”, Talanta. vol. 42, pp.1630-1663, 1995.
[13]. Glasstone, S., Laidler, K. J. and Eyring, H., “The Theory of Rat-Process”, McGraw-Hill, New York. pp.133-139, 1941.
[14]. Gupta, G. and Torres, N., “Use of Fly Ash in Reducing Toxicity of and
Heavy Metals in Wastewater Effluent”, Journal of Hazardous Materials, vol. 57, pp.243-248, 1998.
[15].Gupta, V. K., “Equilibrium Uptake, Sorption Dynamics, Process-
Development, and Column Operations for the Removal of Copper and
Nickel from Aqueous Solution and Wastewater Using Activated Slag, a
Low-Cost Adsorbent”, Industrial and Engineering Chemistry Research,
vol. 37, no. 1, pp.192-202, 1998.
[16]. Gupta, V. K. and Ali, I., “Utilization of Bagasse Fly Ash ( A Sugar Industry Waste) for the Removal of Copper and Zinc from Wastewater”, Separation and Purification Technology, vol. 18, pp.131-140, 2000.
[17]. Hèquet, V., Ricou, P., Lecuyer, I. and Cloirec, P. L., “Removal of Cu 2+ and Zn2+ in Aqueous Solutions by Sorption onto Mixed Fly Ash”, Fuel and Energy Abstracts, vol. 80, pp.851-856, 2001.
[18]. Hsu. Y. C., Wu, F. C. and Tseng, R. L., “ A Study of Activated Clay Adsorbed Dyestuff, Proc. 18th Conf. on Wastewater Treatment Technlolgy”, Taichung, Taiwan, 1993.
[19]. Huang, C. P. and Smith, E. H., “Removal of Cd(II) from Plating Waste Water by An Activated Carbon Process”, Chemistry in Water Reusearch, vol. 2, pp.355-399, 1981.
[20]. Huang, C. P. and Wirth, P. K., “Activated Carbon for Treatment of Cadmium Wastewater”, ASCE Journal of Environmental Engineering, vol. 108, no. 6, pp.1280-1299, 1982.
[21]. Jaycok, M. J., and Parfitt, E. G., “Chemistry of Interfaces”, Ellis, Horwood, New York. pp.265-269, 1981.
[22]. Johonson, B. B., “Effect of pH Temperature and Concen-Tration on the Adsorption of Cadmium on Goethite”, Environmental Science and Technology, vol. 24, pp.112-118, 1990.
[23]. Lopez, E., Soto, B., Arias, M., Nunez, A., Rubinos, A. and Bamal, M., “Adsorption Properties of Red Mud and Its Use for Wastewater Treatment”, Water Research. vol. 32, pp.1314-1322, 1998.
[24]. Low, K. S. and Lee, C. K. “Cadmium Uptake by the Moss Claymepers Delsrtii Bioresour”, Technology vol. 38, pp.1-6, 1991.
[25]. McKay, G., Vong, B. and Porter, J. F., “Isotherm Studies for Theadsorption of Metal Ions onto Peat”, Adsorption Science and Technology, vol. 16, no. 1, pp.51-66, 1997.
[26]. Mckay, G. and Porter, J. R., “Equilibrium Parameters for Thesorption of Copper, Cadmium and Zinc Ions onto Peat”, Journal Chemical Technology and Biotechnology, vol. 69, pp.309-320, 1979.
[27]. Mustafa, S. and Haq, I., “Adsorption of Cu(II), Co(II), and Ni(II) on Amorphous Iron Hydroxide from Aqueous Electrolyte Solution”, Environmental Science and Technology, vol. 9, pp.1379-1386. (1988)
[28]. Namasivayam, C. and Ranganathan, K., “Removal of Cd (H) from Waste Water by Adsorption onto Waste Fe(III)/Cr(III) Hydroxide”, Water Research, vol. 29, pp.1737-1744, 1995.
[29]. Petrucci, R. H., “Spontaneous Change: Entropy and Free Energy”, 5th Ed., Macmillan, New York, pp.714-750, 1989.
[30]. Periasamy, K. and Namasivayam, C., “Process Development for Removal and Recovery of Cadmium from Wastewater by a Low-Cost Adsorbent: Adsorption Rates and Equilibrium Studies”, Industrial Engineering Chemistry Research, vol. 33, pp.317-320, 1994.
[31]. Petrov, N., Budinova, T, and Khaveson, I., “Adsorption of Zinc, Cadmium, Copper and Lead Ions on Oxidized Anthracite”, Carbon, vol. 30, pp.135-139, 1992.
[32]. Panday, K. K., Prasad ,G. and Singh, V. N., “Copper(Ⅱ) Removal from Aqueous Solutions by the Fly Ash”, Water Research, vol. 19 , no. 7, 869-873, 1985.
[33]. Singh, D. and Rawat, N. S., “ Bitumonous Coal for the Treatment of Cd(II)-Rich Water”, Journal Chemical Technology and Biotechnology, vol. 1, pp.266-270, 1994.
[34]. Smith, J. M., Van Ness, H. C. and Abbott, M. M., “Introduction to Chemical Engineering Thermodynamics”, McGrawHill, New York, pp.536-553, 1996.
[35]. Sethurama, V. V. and Raymahashay, B. C., “ Color Removal by Clays Kinetic Study of Adsorption Cationic and Aniunic Dyes”, Environmental Science and Technology, vol. 9, no. 13, pp.1139-1140, 1975.
[36]. Srivastava, S. K., Gupta, V. K. and Mohan, D., “Removal of Lead and Chromium by Activated Slag-A Blast-Furnace Waste ”, ASCE Journal of Environmental Engineering, vol. 123, no. 5, pp.461-468, 1997.
[37]. Sen, A. K. and De, A. K., “Adsorption of Mercury(Ⅱ) by Coal Fly Ash”, Water Research, vol. 21, no. 8, pp.885-888, 1987.
[38]. Spark, K. M., Johnson, B. B. and Wells, J. D., “Characterizing Heavy Metal Adsorption on Oxides and Oxyhydroxides”, European Journal of Soil Science, vol. 46, no. 4, pp.621-631, 1995.
[39]. Svensson, C., “Use or Disposal of By-products and Spent Material from the Vegetable Oil Processing”, Industry in Europe, no. 53, pp.443-445, 1976.
[40]. Tsai, W. T., Hsien, K. J. and Yang, J. M. “Silica Adsorbent Prepared from Spent Diatomaceous Earth and Its Application to Removal of Dye from Aqueous Solutio”, Chia Nan University of Pharmacy and Science, vol. 275, no. 2, pp.428-433, 2004.
[41]. Villaescusa, I., Martinez, M. and Miralles, N., “Heavy Metaluptake from Aqueous Solution by Cork and Yohimbe Bark Wastes”, Journal Chemical Technology and Biotechnology, vol. 75, pp.812-816, 2000.
[42]. Weng, C. H. and Huang, C. P. “Removal of Trace Heavy Metals by Adsorption onto Fly Ash”, Proc., Specialty Conference C. R. O''Melia, ed., ASCE, New York, 923-924, 1990.
[43]. Weng, C. H., Wang, J. H. and Huang, C. P. “Adsorption of Cr(VI) onto TiO2 from Dilute Aqueous Solutions”, Water Science and Technology, vol. 35, no. 7, 55-62, 1997.
[44]. Weng, C. H. and Huang, C. P., “Treatment of Metal Industrial Wastewater by Fly Ash and Cement Fixation”, ASCE Journal of
Environmental Engineering, vol. 120, no.6, pp.1470-1487, 1994.
[45]. Weng, C. H., “Removal of Nickel(II) from Dilute Aqueous Solution by Sludge-Ash”, ASCE Journal of Environmental Engineering, vol. 128, no. 8, pp.716-722, 2002.
[46]. Weng, C. H., Chiang, P. C., and Chang, E. E., “Adsorption Characteristics of CuII onto Industrial Wastewater Sludges”, Adsorption Science & Technology, vol. 19, no. 2, pp.143-158, 2001.
[47]. Yadava, K. P., Tyagi, B. S., Panday, K. K. and Singh, V. N., “Fly ash for the treatment of Cd(II) rich effluents”, Environmental Science and Technology Letters, vol. 8, no. 4, pp.225-234, 1987.
[48]. 王明光(譯),McBride, M. B.(著),“土壤環境化學”,國立編譯館,台北,第77-79頁,1997。
[49]. 王怡敦,“礦物組成對燃煤飛灰去除水中銅離子之影響”,碩士論文,嘉南藥理科技大學,台南,第51-53頁,2003。
[50]. 林敬智,“下水污泥灰渣應用於銅離子去除之初步探討”,碩士論文,國立中央大學,台北,第66-69頁,2000。
[51]. 林介明,“以飛灰去除水中銅、鋅、鉛、鉻之研究”,碩士論文,國立中興大學環境工程研究所,台中,第101-106頁,1998。
[52]. 林建榮,“燃煤飛灰去除水中污染物行為之研究”,博士論文,國立成功大學環境工程研究所,台南,第98-102頁,2001。
[53]. 柯澤豪、李建鴻、胡忠華,“活性碳纖維之發展及其應用”,化工技術,第六卷,第四期,第134-141頁,1998。
[54]. 何寬宏,“垃圾焚化底渣吸附鉻酸離子之可行性研究”,碩士論文,國立成功大學環境工程研究所,台南,第122-125頁,2000。
[55]. 徐永錢、江春喬、王治平,“活性碳混合活性白土吸附酸性染料(AB9)廢水之行為”,第23屆廢水處理技術研討會論文集,第687-693頁,1998。
[56]. 許榮松,“廢白土的處理對策” ,清潔生產雙月刊,第十期,第101-102,1997。
[57]. 陳松甫,“碳化農業廢棄物改良水田重金屬污染之可行性研究”,碩 士論文,國立中興大學土壤環境科學系,台中,第52-54頁,2002。
[58]. 翁誌煌、蔡鑫位,“生物污泥灰對染料(new coccine)的吸附特性研究”第二十五屆廢水處理研討會論文集,高雄,第795-801頁,2000。
[59]. 孫嘉福、李孫榮、楊英賢、廖文彬,“燃煤灰渣去除水中鋅離子可行性之研究 ”,第四屆海峽兩岸環境保護學術研討會論文集,中壢,第835-842頁,1996。
[60]. 楊金鐘、黃靜雯,“垃圾焚化飛灰/反應產物合成沸石之最佳操作條
件探討”,第十四屆廢棄物處理技術論文集,台中,第150-157頁,
1993。
[61]. 楊慶熙,葉芳露,曾德意,陳明輝,黃志峰,李怡萱,王厚傳,謝長良,陳旺,“中小型焚化爐廢氣重金屬控制技術介紹”,工業污染防治,第72期,第82-100頁, 1999。
[62]. 薛文慶,“廢觸媒去除水中金屬之研究”,碩士論文,嘉南藥理科技大學,台南,第93-94頁,2004。
[63]. 經濟部工業局,以水泥窯處理事業廢棄物並回收資源之技術,美國/台灣工業減廢技術轉移研習會,第52-56頁,1995。
[64]. 鄭弘毅,“活性白土處理乳化脂肪酸與染料染整模擬廢水之機構及現象”,碩士論文,國立台灣工業技術學院,台北,第69-72頁,1994。
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