Preface |
|
xv | |
Author |
|
xvii | |
|
1 Occurrence and Importance of Heavy Metal Contamination |
|
|
1 | (28) |
|
|
1 | (2) |
|
|
3 | (2) |
|
1.3 Environmental Importance |
|
|
5 | (5) |
|
1.3.1 Essential Light Metals |
|
|
6 | (1) |
|
1.3.2 Essential Heavy Metals |
|
|
7 | (1) |
|
|
8 | (2) |
|
1.4 Toxicity of Heavy Metals |
|
|
10 | (1) |
|
1.5 Guidelines and Standards for Heavy Metals in Drinking Water |
|
|
10 | (3) |
|
1.6 Sources of Heavy Metal Contamination |
|
|
13 | (2) |
|
|
13 | (1) |
|
|
14 | (1) |
|
|
15 | (1) |
|
1.6.4 Atmospheric Sources |
|
|
15 | (1) |
|
1.7 Important Heavy Metals |
|
|
15 | (11) |
|
|
15 | (3) |
|
|
18 | (1) |
|
|
19 | (2) |
|
|
21 | (1) |
|
|
22 | (2) |
|
|
24 | (1) |
|
|
25 | (1) |
|
|
25 | (1) |
|
|
26 | (1) |
|
|
26 | (1) |
|
|
26 | (1) |
|
|
26 | (3) |
|
2 Pollution Prevention: Principles and Applications |
|
|
29 | (24) |
|
|
29 | (2) |
|
2.2 Motivation and Concept of P2 |
|
|
31 | (2) |
|
|
31 | (1) |
|
|
32 | (1) |
|
|
32 | (1) |
|
2.3 P2 Laws and Regulations |
|
|
33 | (5) |
|
|
38 | (1) |
|
|
39 | (1) |
|
2.6 Pollution Prevention Feasibility |
|
|
40 | (4) |
|
2.6.1 Technical Feasibility |
|
|
40 | (1) |
|
2.6.2 Environmental Feasibility |
|
|
41 | (2) |
|
2.6.3 Economic Feasibility |
|
|
43 | (1) |
|
2.7 P2 Implementation and Revision |
|
|
44 | (1) |
|
2.7.1 Project Implementation |
|
|
44 | (1) |
|
2.7.2 Review and Revision of Project |
|
|
45 | (1) |
|
2.8 Key Points in P2 Applications |
|
|
45 | (5) |
|
2.8.1 Material Handling and Storage |
|
|
45 | (1) |
|
2.8.2 Process Modification |
|
|
46 | (1) |
|
2.8.2.1 Process Variable Controls |
|
|
46 | (1) |
|
2.8.2.2 Replacement with Cleaning Processes |
|
|
46 | (1) |
|
2.8.2.3 Chemical Catalysts |
|
|
47 | (1) |
|
2.8.2.4 Segregation and Separation |
|
|
47 | (1) |
|
2.8.3 In-Process Recycling |
|
|
47 | (1) |
|
2.8.4 Materials and Product Substitutions |
|
|
48 | (1) |
|
2.8.4.1 Materials Substitution |
|
|
48 | (1) |
|
2.8.4.2 Product Substitution |
|
|
48 | (1) |
|
2.8.5 Materials Separation |
|
|
49 | (1) |
|
|
50 | (1) |
|
|
50 | (1) |
|
2.9.2 Water Reduction in Pulp Mill |
|
|
50 | (1) |
|
|
50 | (1) |
|
|
51 | (2) |
|
3 Precipitation Technology |
|
|
53 | (42) |
|
|
53 | (1) |
|
|
54 | (20) |
|
3.2.1 Calculation of Precipitation Reaction |
|
|
54 | (9) |
|
3.2.2 Typical Treatment Reagents |
|
|
63 | (1) |
|
|
63 | (1) |
|
|
64 | (1) |
|
|
65 | (2) |
|
3.2.3 Important Operational Parameters |
|
|
67 | (3) |
|
3.2.4 Treatability of Individual Metals |
|
|
70 | (1) |
|
|
70 | (2) |
|
|
72 | (1) |
|
|
73 | (1) |
|
|
74 | (1) |
|
|
74 | (1) |
|
|
74 | (1) |
|
|
74 | (1) |
|
|
74 | (1) |
|
|
75 | (1) |
|
3.5 Key Devices in Pre- and Posttreatment Steps |
|
|
75 | (10) |
|
3.5.1 Coagulation and Flocculation |
|
|
75 | (1) |
|
|
76 | (5) |
|
|
81 | (1) |
|
3.5.4 Dissolved Air Flotation |
|
|
82 | (1) |
|
3.5.5 Sludge Thickening and Dewatering |
|
|
82 | (2) |
|
|
84 | (1) |
|
|
84 | (1) |
|
3.5.5.3 Compression Filter |
|
|
85 | (1) |
|
3.5.5.4 Centrifuge Device |
|
|
85 | (1) |
|
|
85 | (6) |
|
3.6.1 Treatment of Heavy Metals in Wastewater from Electroplating Operation |
|
|
85 | (2) |
|
3.6.2 Metal Removal by Insoluble Sulfide Precipitation |
|
|
87 | (1) |
|
3.6.3 Hybrid System for Metal Removal |
|
|
88 | (1) |
|
3.6.4 Segregated Treatment of Difficult-To-Treat Metal |
|
|
89 | (1) |
|
3.6.5 Treatment of Arsenic by Precipitation-Coagulation |
|
|
90 | (1) |
|
3.7 Limitations and Solutions |
|
|
91 | (2) |
|
3.7.1 Presence of Chelating Agents |
|
|
91 | (1) |
|
3.7.2 Production of Solids |
|
|
92 | (1) |
|
3.7.3 Importance of Process Control |
|
|
93 | (1) |
|
|
93 | (2) |
|
4 Precipitation-Crystallization Technology |
|
|
95 | (30) |
|
|
95 | (1) |
|
4.2 Description of Technology |
|
|
96 | (1) |
|
4.3 Theoretical Background |
|
|
97 | (4) |
|
4.3.1 Surface Precipitation |
|
|
97 | (1) |
|
4.3.2 Crystallization Kinetics |
|
|
98 | (2) |
|
4.3.2.1 Crystal Nucleation |
|
|
100 | (1) |
|
|
100 | (1) |
|
4.3.2.3 Secondary Changes |
|
|
100 | (1) |
|
4.3.3 Degree of Crystal Dispersion |
|
|
101 | (1) |
|
4.4 Important Control Factors |
|
|
101 | (11) |
|
4.4.1 Total Carbon Concentration versus Metal Concentration |
|
|
103 | (1) |
|
4.4.2 Start-Up of the System |
|
|
103 | (2) |
|
4.4.3 Recycle Ratio and Hydraulic Loading |
|
|
105 | (2) |
|
|
107 | (1) |
|
4.4.5 Lead Loading and Supersaturation |
|
|
107 | (1) |
|
|
108 | (2) |
|
4.4.7 Properties of Sand Grains and Suspended Solids |
|
|
110 | (1) |
|
4.4.7.1 Metal Contents on Sand Grains |
|
|
111 | (1) |
|
4.4.7.2 Microscopic Examination of Lead-Coated Sand Grains |
|
|
111 | (1) |
|
4.4.7.3 Suspended Solids in FBR |
|
|
111 | (1) |
|
|
112 | (11) |
|
|
112 | (1) |
|
4.5.2 Recovery of Ni-Bearing Electroplating Wastewater |
|
|
112 | (1) |
|
4.5.3 Removal of Iron from Acid Mine Drainage |
|
|
112 | (1) |
|
4.5.4 Removal of Multispecies Heavy Metals |
|
|
113 | (3) |
|
4.5.5 Removal of Phosphate |
|
|
116 | (1) |
|
4.5.6 Copper Removal and Recovery |
|
|
117 | (1) |
|
4.5.7 Fluoride Removal and Recovery |
|
|
118 | (2) |
|
|
120 | (3) |
|
|
123 | (2) |
|
5 Reduction-Oxidation Processes |
|
|
125 | (90) |
|
|
125 | (15) |
|
5.2 Chemical-Induced Reduction Processes |
|
|
140 | (16) |
|
|
140 | (1) |
|
|
141 | (2) |
|
|
143 | (4) |
|
5.2.2.2 Effect of Humic Acid |
|
|
147 | (1) |
|
|
148 | (1) |
|
5.2.2.4 Competition in Metal Reduction |
|
|
149 | (1) |
|
5.2.2.5 Effect of Seeding and Aging Process |
|
|
150 | (3) |
|
|
153 | (1) |
|
|
153 | (2) |
|
5.2.5 Other Reducing Reagents |
|
|
155 | (1) |
|
5.3 Biological Reduction of Metal Sulfate |
|
|
156 | (19) |
|
5.3.1 Importance of Sulfate Removal |
|
|
156 | (1) |
|
5.3.2 Mechanisms and Controlling Factors |
|
|
157 | (5) |
|
|
162 | (3) |
|
5.3.2.2 Type of Electron Donors |
|
|
165 | (7) |
|
|
172 | (1) |
|
|
172 | (3) |
|
5.4 Reduction of Hexavalent Chromium |
|
|
175 | (25) |
|
5.4.1 Solution Chemistry of Chromium |
|
|
175 | (1) |
|
5.4.1.1 Hexavalent Chromium |
|
|
175 | (1) |
|
5.4.1.2 Trivalent Chromium |
|
|
176 | (1) |
|
5.4.2 Activated Sludge Process |
|
|
176 | (2) |
|
5.4.3 Membrane Bioreactor |
|
|
178 | (1) |
|
5.4.3.1 Effect of Metal on Membrane Flux |
|
|
179 | (2) |
|
5.4.3.2 Effect of Metal on Sludge Production |
|
|
181 | (1) |
|
5.4.3.3 Effect of Metal on Carbonaceous Pollutant Removal |
|
|
181 | (3) |
|
5.4.3.4 Effect of Metal on Removal of Nutrient |
|
|
184 | (8) |
|
|
192 | (8) |
|
5.5 Reduction and Oxidation of Arsenic Species |
|
|
200 | (8) |
|
|
200 | (1) |
|
5.5.1.1 Chemical Oxidation |
|
|
201 | (2) |
|
5.5.1.2 Catalytic Oxidation |
|
|
203 | (3) |
|
5.5.1.3 Biological Oxidation |
|
|
206 | (1) |
|
|
207 | (1) |
|
|
208 | (7) |
|
6 Electrochemical Technologies for Heavy Metal Decontamination |
|
|
215 | (40) |
|
|
215 | (1) |
|
6.2 Electrodeposition Technology |
|
|
216 | (16) |
|
6.2.1 Typical Reaction at Electrodes |
|
|
216 | (1) |
|
6.2.1.1 Reduction Reactions at Cathode |
|
|
216 | (1) |
|
6.2.1.2 Oxidation Reactions at Anode |
|
|
217 | (1) |
|
6.2.2 Factors Affecting Electrodeposition |
|
|
217 | (1) |
|
6.2.2.1 Effect of Initial Concentration |
|
|
218 | (2) |
|
6.2.2.2 Effect of Distance between Electrodes |
|
|
220 | (1) |
|
|
220 | (1) |
|
|
220 | (3) |
|
|
223 | (2) |
|
6.2.2.6 Effect of Ionic Strength |
|
|
225 | (2) |
|
6.2.3 Recovery of Multicomponent Metal Ions |
|
|
227 | (3) |
|
6.2.4 Industrial Application |
|
|
230 | (2) |
|
6.3 Electrocoagulation and Electroflotation |
|
|
232 | (19) |
|
|
232 | (1) |
|
6.3.1.1 Conventional Coagulation |
|
|
232 | (1) |
|
|
233 | (1) |
|
6.3.1.3 Typical Electrode Connection |
|
|
233 | (1) |
|
6.3.1.4 Electrode Reactions |
|
|
234 | (1) |
|
6.3.1.5 Factors Influencing EC |
|
|
234 | (1) |
|
|
235 | (1) |
|
6.3.2.1 Selection of Electrodes |
|
|
236 | (1) |
|
|
236 | (1) |
|
6.3.2.3 Factors Affecting EF |
|
|
237 | (1) |
|
6.3.3 Combination of EC and EF |
|
|
237 | (1) |
|
|
237 | (1) |
|
|
238 | (1) |
|
6.3.3.3 Cell Arrangements |
|
|
239 | (2) |
|
|
241 | (1) |
|
|
241 | (1) |
|
|
242 | (3) |
|
|
245 | (3) |
|
|
248 | (1) |
|
6.3.4.5 Removal of Heavy Metals from Saline Leachate |
|
|
248 | (1) |
|
6.3.4.6 Nickel and Zinc Removal |
|
|
248 | (1) |
|
|
249 | (1) |
|
6.3.4.8 A Hybrid EC/EF-Membrane Process |
|
|
249 | (2) |
|
|
251 | (4) |
|
7 Adsorption: Materials, Chemistry, and Applications |
|
|
255 | (98) |
|
|
255 | (2) |
|
|
257 | (46) |
|
|
257 | (4) |
|
|
261 | (2) |
|
7.2.3 Types of Metal Ions |
|
|
263 | (2) |
|
7.2.4 Effect of Ionic Strength |
|
|
265 | (2) |
|
7.2.5 Effect of Background Electrolyte |
|
|
267 | (1) |
|
7.2.6 Effect of Initial Concentration and Dosage |
|
|
268 | (1) |
|
7.2.7 Adsorption Isotherm |
|
|
269 | (1) |
|
7.2.8 Presence of Industrial Organic Matters |
|
|
269 | (9) |
|
7.2.9 Effect of Natural Organic Matters |
|
|
278 | (8) |
|
7.2.10 Effect of Surfactant |
|
|
286 | (5) |
|
7.2.11 Effect of Competing Ions |
|
|
291 | (2) |
|
7.2.12 Temperature Effect |
|
|
293 | (1) |
|
7.2.13 Effect of Carbon Type |
|
|
294 | (1) |
|
7.2.14 Modification of Activated Carbon |
|
|
295 | (1) |
|
7.2.14.1 Chemical Approaches |
|
|
296 | (1) |
|
7.2.14.2 Physical Approaches |
|
|
296 | (1) |
|
7.2.14.3 Metal Performance of Modified Activated Carbons |
|
|
297 | (6) |
|
|
303 | (25) |
|
7.3.1 Preparation of Biosorbents |
|
|
303 | (10) |
|
7.3.2 Biosorption Chemistry |
|
|
313 | (2) |
|
7.3.3 Biosorption Performance |
|
|
315 | (13) |
|
|
328 | (10) |
|
7.5 Adsorption Treatment System |
|
|
338 | (3) |
|
7.5.1 Fluidized Bed Reactor |
|
|
338 | (1) |
|
7.5.2 Stirred Tank Reactor |
|
|
338 | (1) |
|
|
339 | (2) |
|
|
341 | (12) |
|
8 Calculation of Metal Ion Uptake in Environmental Systems |
|
|
353 | (50) |
|
|
353 | (16) |
|
|
354 | (7) |
|
8.1.2 Freundlich Equation |
|
|
361 | (1) |
|
|
362 | (1) |
|
8.1.4 Dubinin-Raduskevich Adsorption Model |
|
|
362 | (1) |
|
8.1.5 Redlich-Peterson Model |
|
|
363 | (1) |
|
|
363 | (1) |
|
8.1.7 Multicomponent Isotherms |
|
|
364 | (1) |
|
8.1.8 Surface Complex Formation Model |
|
|
365 | (1) |
|
8.1.8.1 Model Description |
|
|
365 | (2) |
|
8.1.8.2 Surface Complex Formation Reactions |
|
|
367 | (2) |
|
|
369 | (7) |
|
|
376 | (2) |
|
8.3.1 Metal Uptake by Biosorbent |
|
|
376 | (1) |
|
8.3.2 Metal Uptake by Composite Sorbent |
|
|
377 | (1) |
|
8.4 Equilibrium Calculation by Computational Tools |
|
|
378 | (4) |
|
|
378 | (1) |
|
8.4.2 Mathematical Description |
|
|
379 | (2) |
|
8.4.3 Determination of Model Parameters |
|
|
381 | (1) |
|
8.5 Case Studies of Adsorption Equilibrium |
|
|
382 | (16) |
|
8.5.1 Heavy Metal Adsorption onto Activated Carbon |
|
|
382 | (1) |
|
8.5.1.1 Surface Charge Properties |
|
|
382 | (4) |
|
8.5.1.2 Adsorption of Heavy Metals |
|
|
386 | (3) |
|
8.5.1.3 Multiple-Species Metal Ion Adsorption |
|
|
389 | (2) |
|
8.5.2 Heavy Metal Sorption onto a Calcium-Alginate Encapsulated Magnetic Sorbent |
|
|
391 | (3) |
|
8.5.2.1 Interaction of Functional Groups, Calcium, and Hydrogen Ions |
|
|
394 | (3) |
|
8.5.2.2 Interaction of Functional Groups and Heavy Metal Ions |
|
|
397 | (1) |
|
8.5.2.3 Prediction of pH Effect |
|
|
397 | (1) |
|
8.6 Modeling of Adsorption Kinetics |
|
|
398 | (5) |
|
8.6.1 Surface Diffusion Control Model |
|
|
399 | (1) |
|
8.6.2 Pore Diffusion Control Model |
|
|
400 | (3) |
Appendix A Introduction of MINEQL Modeling |
|
403 | (3) |
Appendix B Empirical Kinetics Model |
|
406 | (11) |
Appendix C Surface Diffusion Model |
|
417 | (2) |
References |
|
419 | (6) |
Index |
|
425 | |