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1. | Introduction | 1 |
2. | Production-Integrated Environmental Protection in the Chemical Industry | 5 |
2.1. | Chemical Industry and Sustainable Development | 5 |
2.2. | Formation of Residues in Chemical Processes | 6 |
2.3. | Environmental Concepts in the Chemical Industry | 9 |
2.3.1. | Review of the Environmental Concepts | 9 |
2.3.2. | The Concept of Integrated Environmental Protection | 10 |
2.3.3. | Environmental Protection in Research and Development | 11 |
2.3.4. | Integrated and Additive Concepts of Environmental Protection | 12 |
2.3.5. | Comparison of Integrated and Additive Environmental Protection | 15 |
2.3.6. | Methods of material flow and cost management | 21 |
2.4. | Limitations of Production-Integrated Environmental Protection | 27 |
2.4.1. | Technical Limitations | 28 |
2.4.2. | Economic Limitations | 29 |
2.5. | Effect of Production-Integrated Environmental Protection | 29 |
2.6. | Costs of Integrated Measures | 31 |
3. | Examples of Production-Integrated Environmental Protection in the Chemical Industry | 33 |
3.1. | Introduction | 33 |
3.2. | Selected Examples | 34 |
3.2.1. | Examples from Hoechst | 34 |
3.2.1.1. | Recovery and Utilization of Residues in the Production of Viscose Staple Fiber | 34 |
3.2.1.2. | Recovery of Methanol and Acetic Acid in Poly (Vinyl Alcohol) Production | 40 |
3.2.1.3. | Acetylation without Contamination of Wastewater | 40 |
3.2.1.4. | Reutilization Plant for Organohalogen Compounds | 41 |
3.2.1.5. | Vacuum Technology for Closed Production Cycles | 45 |
3.2.1.6. | Utilization of Exhaust Gases and Liquid Residues of Chlorination Processes for Production of Clean Hydrochloric Acid Hydrochloric Acid Hydrochloric Acid Hydroc | 47 |
3.2.1.7. | Production of Neopentyl Glycol: Higher Yield by Internal Recycling | 50 |
3.2.1.8. | Optimization of Ester Waxoil Production and Recovery of Auxiliary Products | 51 |
3.2.1.9. | Biochemical Production of 7-Aminocephalosporanic Acid | 53 |
3.2.1.10. | Production of | 56 |
3.2.1.11. | Production of Theobromine | 57 |
3.2.1.12. | Recovery of Organic Solvents | 59 |
3.2.2. | Examples from Bayer | 67 |
3.2.2.1. | Avoidance of Wastewater and Residues in the Production of H Acid (1-Amino-8-hydroxynaphthalene-3,6-disulfonic acid) | 67 |
3.2.2.2. | High-Yield Production of Alkane-sulfonates by Means of Membrane Technology | 71 |
3.2.2.3. | Selective Chlorination of Toluene in the | 73 |
3.2.2.4. | Production of Naphthalenedisulfonic Acid with Closed Recycling of Auxiliaries | 75 |
3.2.2.5. | Avoiding Residues in Dye Production by Using Membrane Processes | 80 |
3.2.2.6. | Fuel Replacement in Sewage Sludge Combustion by Utilization of Chlorinated Hydrocarbon Side Products | 81 |
3.2.3. | Examples from BASF | 84 |
3.2.3.1. | Emission Reduction in Industrial Power Plants at Chemical Plant Sites by Means of Optimized Cogeneration | 84 |
3.2.3.2. | Closed-Cycle Wittig Reaction | 90 |
3.2.4. | Integrated Environmental Protection and Energy Saving in the Production of Vinyl Chloride (Example from Wacker Chemie) | 93 |
3.2.5. | Examples from Huls | 104 |
3.2.5.1. | Integrated Environmental Protection in Cumene Production | 104 |
3.2.5.2. | Production of Acetylene by the Huls Plasma Arc Process | 107 |
3.2.6. | Low-Residue Process for Titanium Dioxide Production (Example from Kronos International) | 111 |
3.2.7. | Reduction of Waste Production and Energy Consumption in the Production of Fatty Acid Methyl Esters (Example from Henkel) | 115 |
3.2.8. | Integrated Environmental Protection in the Production of Vitamins (Example from F. Hoffmann-La Roche) | 122 |
3.2.9. | Production of Pure Naphthalene without Residues--Replacement of Chemical Purification by Optimized Multiple Crystallization (Example from | 128 |
3.2.10. | Improvements in the Polypropylene Production Process (Example from Shell) | 132 |
3.2.11. | The Zero-Residue Refinery Using the Shell Gasification Process (Shell-Lurgi Example) | 135 |
3.2.12. | Neutral Salt Splitting with the Use of Hydrogen Depolarized Anodes (Hydrina Technology, Example from De Nora Permelec) | 142 |
3.2.13. | Ultrapure Isopropanol Purification and Recycling System (Example from Mitsubishi Chemical) | 151 |
3.2.14. | Examples from Boehringer Mannheim | 156 |
3.2.14.1. | Biocatalytic Splitting of Penicillin | 156 |
3.2.14.2. | Production of Diagnostic Reagents by Means of Genetic Engineering: Glucose-6-Phosphate Dehydrogenase and | 158 |
4. | Waste Management in the Chemical Industry | 163 |
4.1. | Introduction | 163 |
4.2. | Chemical Industry Wastes | 163 |
4.3. | Waste-Management Concepts | 164 |
4.3.1. | Residues and Wastes from Production | 164 |
4.3.2. | Production-Oriented Management | 165 |
4.3.3. | Product-Oriented Management | 166 |
4.4. | Disposal Measures | 167 |
4.4.1. | Logistics | 167 |
4.4.2. | Waste Combustion | 168 |
4.4.3. | Landfill Disposal of Wastes | 173 |
4.4.4. | Asbestos Disposal | 174 |
4.5. | Utilization of Product Wastes | 174 |
4.5.1. | Plastics Recycling | 174 |
4.5.2. | Refrigerant Recycling | 176 |
4.5.3. | Recycling of Used Packaging Materials | 177 |
4.5.4. | Paint Recycling | 178 |
4.6. | Results of Waste Management | 178 |
5. | Summary and Outlook | 183 |
6. | References | 185 |
Index | 197 |
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