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Book Details
Abstract
Phosphorus has always been both a curse and a blessing. On the one hand, it is essential for all life forms and cannot be replaced by anything. On the other hand, wastewater treatment aims to minimize phosphorus concentrations in wastewater in order to minimize its discharge into rivers and lakes, where eutrophication caused by high phosphorus concentrations would lead to excessive plant growth. Phosphorus is extracted from rock phosphate deposits, which are finite and non-renewable. And as the issue of resource conservation is the focus of attention worldwide, phosphorus must be used sustainably. This includes recycling of secondary phosphates, efficient extraction and treatment of raw phosphate as well as its efficient use.
The book starts from the peculiarity of the element phosphorus in Part I Phosphorus a special element?, Part II shows the possibilities and limitations of the elimination of phosphorus during the wastewater treatment. Current developments in phosphorus recovery are presented in Part III Phosphorus Recovery - Technology, where also a large number of technology developments are presented in the context of case studies. Part IV “Assessment” shows impulses for future ways. The book concludes with an “Outlook” in Part V.
The book is partially based on the book Phosphorus in Environmental Technology – Principles and Application, edited by Eugina Valsami-Jones and published by IWA Publishing in 2004. Various new technologies have been developed since its release, particularly in the area of phosphorus recovery. Phosphorus: Polluter and Resource of the Future discusses all aspects of both Phosphorus elimination and recovery and summarizes the latest state of Phosphorus recovery technologies.
Table of Contents
Section Title | Page | Action | Price |
---|---|---|---|
Cover | Cover | ||
Contents | v | ||
About the Editor | xxi | ||
Preface – Phosphorus: Curse and Blessing? | xxiii | ||
Part I: Phosphorus – A Special Element | 1 | ||
Chapter 1: Phosphorus the pollutant | 3 | ||
1.1 INTRODUCTION | 3 | ||
1.2 PERCEPTIONS OF PHOSPHORUS AS A POLLUTANT | 5 | ||
1.3 REACTIVE P FROM RURAL ENVIRONMENTS | 9 | ||
1.3.1 The phosphorus transfer continuum | 9 | ||
1.3.1.1 Legacy soil phosphorus | 13 | ||
1.3.1.2 Fresh phosphorus amendments | 13 | ||
1.3.1.3 Other rural phosphorus sources | 14 | ||
1.4 REACTIVE P FROM URBAN ENVIRONMENTS | 14 | ||
1.4.1 Urban wastewater discharges | 15 | ||
1.4.2 Urban stormwater run-off | 16 | ||
1.5 ARE ALL SOURCES OF PHOSPHORUS EQUALLY POLLUTING? | 16 | ||
1.5.1 Ecological relevance of phosphorus forms | 17 | ||
1.6 CONTROL OF PHOSPHORUS POLLUTION | 19 | ||
1.6.1 Point source controls | 19 | ||
1.6.2 Diffuse source controls | 20 | ||
1.7 STRATEGIES TOWARDS MORE SUSTAINABLE PHOSPHORUS USE | 21 | ||
1.8 CONCLUSIONS | 22 | ||
1.9 REFERENCES | 23 | ||
Chapter 2: Phosphate pollution: A global overview of the problem | 35 | ||
2.1 INTRODUCTION | 35 | ||
2.2 THE EUROPEAN UNION | 38 | ||
2.3 THE UNITED STATES | 44 | ||
2.4 AUSTRALIA | 45 | ||
2.5 JAPAN | 47 | ||
2.6 SOUTH AND EAST ASIA | 49 | ||
2.7 AFRICA | 51 | ||
2.8 ANTARCTICA | 52 | ||
2.9 CONCLUSIONS | 52 | ||
2.10 REFERENCES | 53 | ||
Chapter 3: Phosphorus as a resource | 57 | ||
3.1 INTRODUCTION | 57 | ||
3.2 PHOSPHORUS FLOW ANALYSIS | 58 | ||
3.2.1 Phosphorus flows in Europe | 58 | ||
3.2.1.1 System description and assumptions | 58 | ||
3.2.1.2 Human phosphorus consumption | 59 | ||
3.2.1.3 Phosphorus flows by sector | 60 | ||
3.2.1.4 Phosphorus sinks and losses | 62 | ||
3.2.2 Global phosphorus flows | 63 | ||
3.2.2.1 The supply–demand chain for mined phosphorus | 63 | ||
3.2.2.2 Additional inputs | 65 | ||
3.2.2.3 Losses | 65 | ||
3.2.2.4 Efficiency of phosphate rock use | 67 | ||
3.3 MINERAL PHOSPHORUS RESOURCES AND RESERVES | 70 | ||
3.3.1 Definition of resources and reserves | 70 | ||
3.3.1.1 Current reserves and resources | 70 | ||
3.3.1.2 Recent development of resources and reserves | 71 | ||
3.3.1.3 Physical scarcity and peak phosphorus | 72 | ||
3.4 THE PROBLEM WITH TODAY’S GLOBAL PHOSPHORUS FLOWS | 74 | ||
3.4.1 Economic scarcity | 74 | ||
3.4.2 Environmental pollution | 75 | ||
3.4.3 Providing phosphorus for future generations | 76 | ||
3.4.4 Regional differences in phosphorus balances | 76 | ||
3.5 CONCLUSIONS | 77 | ||
3.6 REFERENCES | 77 | ||
Part II: Elimination of Phosphorus from Wastewater | 81 | ||
Chapter 4: Phosphorus in wastewater | 83 | ||
4.1 ORIGIN OF PHOSPHORUS IN WASTEWATER | 83 | ||
4.2 CONCENTRATION AND LOAD OF PHOSPHORUS IN MUNICIPAL AND INDUSTRIAL WASTEWATER | 88 | ||
4.2.1 Domestic wastewater | 88 | ||
4.2.2 Wastewater from industrial and commercial sources | 92 | ||
4.3 CHEMICAL ANALYSIS OF PHOSPHORUS IN WASTEWATER AND SLUDGE | 93 | ||
4.3.1 Speciation of phosphorus | 93 | ||
4.3.2 Determination of phosphorus in water and wastewater | 97 | ||
4.3.2.1 Manual and semi-automated analyses based on the ascorbic acid method | 99 | ||
4.3.2.2 Automated determination of phosphate | 100 | ||
4.3.2.3 Extraction of phosphorus from sludges using aqua regia | 103 | ||
4.3.2.4 Determination of phosphorus in raw sludge and digested sludge | 104 | ||
4.3.3 Sequential extraction procedures to determine the binding form of phosphorus | 104 | ||
4.3.4 Determination of phosphonates | 105 | ||
4.4 REFERENCES | 105 | ||
Chapter 5: Phosphorus removal in wastewater treatment plants | 109 | ||
5.1 BIOLOGICAL PHOSPHORUS REMOVAL | 109 | ||
5.1.1 Process configurations for EBPR | 110 | ||
5.1.1.1 Anaerobic/oxic (Phoredox and A/O) system | 111 | ||
5.1.1.2 PhoStrip process | 111 | ||
5.1.1.3 Three-stage modified Bardenpho and A2/O system | 111 | ||
5.1.1.4 Five-stage modified Bardenpho | 112 | ||
5.1.1.5 University of Cape Town (UCT) and Virginia Initiative Plant (VIP) processes | 112 | ||
5.1.1.6 Johannesburg and Westbank processes | 113 | ||
5.1.1.7 Time-cyclic processes | 113 | ||
5.1.2 Factors affecting performance | 113 | ||
5.1.2.1 Influent characteristics | 113 | ||
5.1.2.2 Integrity of the anaerobic zone | 114 | ||
5.1.2.3 Aerobic zone impacts | 116 | ||
5.1.2.4 pH | 117 | ||
5.1.2.5 Solids and hydraulic retention times | 117 | ||
5.1.2.6 Temperature | 117 | ||
5.1.2.7 Solids capture | 118 | ||
5.1.2.8 Secondary release and recycle load management | 118 | ||
5.2 CHEMICAL PHOSPHORUS REMOVAL | 118 | ||
5.2.1 Process principles | 119 | ||
5.2.2 Mechanisms of chemical phosphorus removal | 120 | ||
5.2.2.1 Phosphorus species | 121 | ||
5.2.2.2 Reactions with coagulants | 122 | ||
5.2.2.3 Simultaneous phosphorus precipitation | 126 | ||
5.2.2.4 Sequential phosphorus precipitation | 128 | ||
5.2.3 Applications of chemical phosphorus removal | 128 | ||
5.3 REFERENCES | 129 | ||
Chapter 6: Total solids and phosphorus: A cross-linked topic? | 133 | ||
6.1 NECESSITY OF ADVANCED PHOSPHORUS AND PARTICLE REMOVAL | 133 | ||
6.2 PHOSPHORUS AND PARTICLES | 134 | ||
6.3 PROCESSES OF ADVANCED P-ELIMINATION | 136 | ||
6.4 PROCESSES OF SOLID REMOVAL | 137 | ||
6.4.1 Overview of separation processes | 137 | ||
6.4.2 Sedimentation, lamella separator, flotation in combination with post-precipitation | 137 | ||
6.4.3 Filtration processes | 139 | ||
6.4.3.1 Overview of different filtration technologies | 139 | ||
6.4.3.2 Dimensioning of granular wastewater filtration | 141 | ||
6.4.4 Shallow bed filtration | 141 | ||
6.4.4.1 Shallow bed with granular media | 141 | ||
6.4.4.2 Microstrainer | 142 | ||
6.4.4.3 Cloth media filter | 143 | ||
6.4.5 Deep bed filtration | 144 | ||
6.4.6 Membrane filtration | 146 | ||
6.5 ASSESSMENT OF THE DIFFERENT PARTICLE SEPARATION PROCESSES | 147 | ||
6.6 REFERENCES | 148 | ||
Chapter 7: Effects of phosphorus removal in wastewater on sludge treatment processes and sludge dewatering | 151 | ||
7.1 INTRODUCTION | 151 | ||
7.2 DETERMINATION OF DEWATERABILITY OF SEWAGE SLUDGES | 152 | ||
7.3 IMPACT OF WAS AND BIOLOGICAL P-REMOVAL ON SLUDGE DEWATERING | 158 | ||
7.4 ALTERNATIVE FOR MITIGATING THE IMPACT OF EBPR ON DEWATERING | 164 | ||
7.4.1 Phosphate reduction through metal salt addition | 165 | ||
7.4.2 Stored phosphorus release | 165 | ||
7.4.3 Thermal and chemical thermal cell lysis | 168 | ||
7.4.4 Struvite precipitation | 169 | ||
7.5 SUMMARY | 171 | ||
7.6 REFERENCES | 171 | ||
Chapter 8: Phosphorus removal and recovery in focus of a holistic wastewater treatment of the future | 175 | ||
8.1 INTRODUCTION | 175 | ||
8.2 APPROACHES FOR IMPROVED BIOLOGICAL PHOSPHORUS REMOVAL AND SUBSEQUENT RECOVERY | 177 | ||
8.2.1 Kinetic values of conventional biological phosphorus removal | 177 | ||
8.2.2 Optimization of classical biological phosphorus removal | 179 | ||
8.2.3 Membrane processes | 181 | ||
8.2.4 Alternative microorganisms and metabolic processes for phosphorus fixation | 182 | ||
8.3 INNOVATIVE METHODS FOR IMPROVED INTERFACES BETWEEN PHOSPHORUS REMOVAL AND RECYCLATE PRODUCTION | 183 | ||
8.3.1 Microbial fuel cell | 183 | ||
8.3.2 Algae and macrophyte cultures (aquatic plants) | 184 | ||
8.3.3 Use of enzymes/proteins | 185 | ||
8.3.4 Bioleaching | 186 | ||
8.3.5 P-mobilization by bacterial colonization | 187 | ||
8.3.6 Plant systems for heavy metal depletion | 188 | ||
8.3.7 Fungi or mycorrhiza | 189 | ||
8.4 EMERGING PROCESS DESIGNS AND THEIR IMPACT ON PHOSPHORUS REMOVAL AND RECOVERY | 189 | ||
8.4.1 Characterization of phosphorus compounds occurring in wastewater treatment | 190 | ||
8.4.2 Exemplary treatment concepts and their effect on phosphorus removal and recovery | 192 | ||
8.4.2.1 Scenario 0: Conventional biological wastewater treatment with P removal by precipitation (state of the art) | 193 | ||
8.4.2.2 Scenario 1: Conventional biological wastewater treatment enhanced biological P-removal and P-redissolution from surplus | 194 | ||
8.4.2.3 Scenario 2: “Main stream deammonification” for nitrogen removal and effluent filtration | 196 | ||
8.4.3 Comparison and evaluation of phosphorus removal concepts in WWTPs of the future | 198 | ||
8.5 REFERENCES | 200 | ||
Chapter 9: Phosphorus removal: An economic assessment | 205 | ||
9.1 INTRODUCTION | 205 | ||
9.2 BACKGROUND ON PHOSPHORUS REMOVAL | 205 | ||
9.3 FACTORS AFFECTING COSTS OF PHOSPHORUS REMOVAL | 206 | ||
9.4 ECONOMIC ASSESSMENT OF DIFFERENT SYSTEMS | 207 | ||
9.5 COSTS OF PHOSPHORUS REMOVAL | 208 | ||
9.5.1 Introduction | 208 | ||
9.5.2 Capital costs (simultaneous precipitation) | 210 | ||
9.5.3 Capital costs (enhanced biological phosphorus removal) | 212 | ||
9.5.4 Capital costs (filtration) | 213 | ||
9.5.5 Capital costs (summary) | 214 | ||
9.5.6 Operational costs | 215 | ||
9.5.7 Lifecycle costs | 216 | ||
9.6 SUMMARY | 217 | ||
9.7 REFERENCES | 217 | ||
Chapter 10: Modeling the phosphorus cycle in the wastewater treatment process | 219 | ||
10.1 INTRODUCTION | 219 | ||
10.1.1 Phosphorus transformations in wastewater treatment | 220 | ||
10.2 MODELING PHOSPHORUS TRANSFORMATIONS | 223 | ||
10.2.1 Biological transformations in mainline | 223 | ||
10.2.2 Anaerobic transformations in sidestream | 225 | ||
10.2.3 Chemical transformations | 226 | ||
10.2.3.1 General chemistry modeling | 227 | ||
10.2.3.2 Water line: coagulation and flocculation with iron and alum | 227 | ||
10.2.3.3 Sludge line: precipitation with calcium, magnesium and iron | 229 | ||
10.3 PLANT-WIDE MODELING OF PHOSPHORUS | 230 | ||
10.3.1 Modeling interactions with iron and sulfur cycles | 230 | ||
10.3.2 Implementation and solution in a plant-wide context | 232 | ||
10.4 PERSPECTIVES AND CHALLENGES | 233 | ||
10.4.1 Modeling challenges | 233 | ||
10.4.2 Enhancing phosphorus recovery | 233 | ||
10.5 CONCLUSIONS | 234 | ||
10.6 REFERENCES | 234 | ||
Part IIIa: Phosphorus Recovery: Technology | 239 | ||
Chapter 11: Wastewater as a resource: From rare earth metals to phosphorus | 241 | ||
11.1 INTRODUCTION | 241 | ||
11.2 ELEMENTAL COMPOSITION OF SEWAGE SLUDGE | 243 | ||
11.3 GERMAN SURVEY OF SEWAGE SLUDGE ASHES | 244 | ||
11.4 REFERENCES | 250 | ||
Chapter 12: From push to pull: Coupling the diverse phosphorus products to the market | 253 | ||
12.1 INTRODUCTION | 253 | ||
12.1.1 A new product in an existing market | 253 | ||
12.1.2 From supply driven to demand driven | 254 | ||
12.2 STAKEHOLDERS IN SUPPLY CHAIN | 255 | ||
12.2.1 The supply chain | 255 | ||
12.2.2 Suppliers | 255 | ||
12.2.3 Users | 256 | ||
12.2.3.1 Aggregators/raw material processors | 256 | ||
12.2.3.2 End-users | 257 | ||
12.2.4 Service providers | 258 | ||
12.2.5 Policymakers | 258 | ||
12.3 MEETING DEMAND | 259 | ||
12.3.1 General requirements demand | 259 | ||
12.3.1.1 Chemical properties | 259 | ||
12.3.1.2 Biochemical properties | 260 | ||
12.3.1.3 Physical properties | 261 | ||
12.3.1.4 Legal status | 261 | ||
12.3.1.5 Security of supply | 262 | ||
12.3.2 Summary requirements | 262 | ||
12.4 TOWARDS PULL: WHAT TO DO? | 263 | ||
12.4.1 Choosing and creating supply chain | 263 | ||
12.4.2 Top products | 263 | ||
12.4.3 Visibility and accessibility of product | 267 | ||
12.4.4 The contract | 267 | ||
12.4.5 Closed a contract: now what? | 267 | ||
12.5 REFERENCES | 268 | ||
Chapter 13: Phosphorus recovery – the North American perspective | 269 | ||
13.1 INTRODUCTION | 269 | ||
13.2 KEY DRIVERS AND BARRIERS | 269 | ||
13.3 TECHNOLOGY REVIEW | 270 | ||
13.3.1 Fluidized bed reactor | 271 | ||
13.3.2 Waste activated sludge stripping to recover internal phosphate (WASSTRIP®) | 274 | ||
13.3.3 AirPrex™ | 274 | ||
13.4 MARKET ANALYSIS | 275 | ||
13.5 CASE STUDIES | 278 | ||
13.6 CONCLUSION | 278 | ||
13.7 REFERENCES | 278 | ||
Chapter 14: The current situation regarding phosphorus recovery in Asian countries | 281 | ||
14.1 PHOSPHORUS DEMAND IN THE ASIA REGION | 281 | ||
14.1.1 The phosphorus flow in China | 283 | ||
14.1.2 The phosphorus flow in Korea | 285 | ||
14.1.3 The phosphorus flow in Taiwan | 286 | ||
14.1.4 The phosphorus flow in Thailand | 286 | ||
14.1.5 The phosphorus flow in Vietnam | 288 | ||
14.1.6 The phosphorus flow in Japan | 289 | ||
14.2 CHALLENGES FOR PHOSPHORUS RECOVERY FROM THE JAPANESE SEWERAGE SYSTEM | 290 | ||
14.2.1 Phosphorus recovery technologies | 291 | ||
14.2.1.1 Recovery from wastewater and/or rejected water | 291 | ||
14.2.2 Phosphorus recovery from sewage sludge | 295 | ||
14.2.3 Phosphorus recovery from incineration ash | 296 | ||
14.2.4 Phosphorus recovery from a melting process | 297 | ||
14.3 CONCLUDING REMARKS | 299 | ||
14.4 REFERENCES | 300 | ||
Chapter 15: New research ideas for phosphorus recovery from wastewater and sewage sludge ash | 305 | ||
15.1 INTRODUCTION | 305 | ||
15.2 NEW FIRST GENERATION PROCESSES | 309 | ||
15.2.1 ExtraPhos® – chemical phosphate recovery from sewage sludge by CO2 acidulation and precipitation | 309 | ||
15.2.1.1 Raw materials | 310 | ||
15.2.1.2 Conclusion and outlook | 310 | ||
15.2.2 Chemical phosphate recovery by functionalized superparamagnetic particles | 311 | ||
15.2.2.1 Conclusion and outlook | 312 | ||
15.2.3 Sequential electrodialytic phosphorus recovery from sewage sludge ash | 312 | ||
15.2.3.1 Applying ED to frozen SS | 313 | ||
15.2.3.2 Applying ED to fresh SS | 313 | ||
15.2.3.3 Applying ED to SSA from low-temperature gasification | 314 | ||
15.2.3.4 Applying ED to SSA incineration | 315 | ||
15.2.3.5 Conclusion and outlook | 315 | ||
15.2.4 Thermal white phosphorus extraction from sewage sludge ash | 315 | ||
15.2.4.1 Introduction to thermal phosphate processing | 315 | ||
15.2.4.2 Thermal processing of secondary raw materials | 317 | ||
15.2.4.3 RecoPhos P4 process | 317 | ||
15.2.4.3.1 Background | 317 | ||
15.2.4.3.2 Process description | 318 | ||
15.2.4.3.3 Raw materials | 319 | ||
15.2.4.3.4 Pilot plant and test work | 320 | ||
15.2.4.3.5 Conclusion | 320 | ||
15.3 SECOND GENERATION PROCESSES | 320 | ||
15.3.1 Nutrient recycling (N + P) by enhanced (microbial) biomass production and nitrogen conservation | 320 | ||
15.3.2 Nutrient (N + P) recycling by microalgae and mixed microbial cultures to fish and fish products | 321 | ||
15.3.3 Nutrient recycling from wastewater by lithoautotrophic (aerobic hydrogen oxidizing) bacteria | 324 | ||
15.3.3.1 Rethinking sewage treatment – the Power-to-Protein concept (www.powertoprotein.eu) | 327 | ||
15.4 SUMMARY AND CONCLUSION | 329 | ||
15.5 REFERENCES | 329 | ||
Part IIIb: Phosphorus Recovery: Technology | 333 | ||
Chapter 16: The Crystalactor® at the WWTP Geestmerambacht (The Netherlands) | 335 | ||
16.1 INTRODUCTION | 335 | ||
16.2 PROCESS DESCRIPTION | 336 | ||
16.2.1 Process scheme | 336 | ||
16.2.2 Chemistry | 337 | ||
16.2.3 Crystalactor® | 338 | ||
16.3 RESULTS OF THE LARGE-SCALE IMPLEMENTATION | 338 | ||
16.3.1 Performance data | 339 | ||
16.3.2 Costs | 339 | ||
16.3.3 Conclusion | 340 | ||
16.3.4 Fact sheet | 340 | ||
16.4 REFERENCES | 341 | ||
Chapter 17: AirPrex® sludge optimization and struvite recovery from digested sludge | 343 | ||
17.1 THEMATIC INTRODUCTION | 343 | ||
17.2 PROCEDURAL DEFINITION | 344 | ||
17.3 ANAEROBIC REDISSOLUTION OF PHOSPHORUS | 345 | ||
17.4 THE INFLUENCE OF STRUVITE PRECIPITATION ON THE TREATMENT OF DIGESTED SLUDGE | 346 | ||
17.4.1 Influence on unwanted struvite crystallizations | 346 | ||
17.4.2 Influence on sludge dewatering | 346 | ||
17.5 THE AIRPREX® PROCESS | 347 | ||
17.6 STRUVITE PRECIPITATION BASED ON THE EXAMPLE OF THE RWZI IN AMSTERDAM-WEST [5] | 348 | ||
17.7 CONCLUSION | 350 | ||
17.8 REFERENCES | 350 | ||
Chapter 18: The PHOSPAQ™ process | 351 | ||
18.1 INTRODUCTION | 351 | ||
18.2 THE PROCESS | 352 | ||
18.2.1 Description | 352 | ||
18.2.1.1 Product | 352 | ||
18.2.1.2 Case Study: Waterstromen Olburgen (The Netherlands) | 353 | ||
18.2.2 Key figures of the process | 356 | ||
18.3 OUTLOOK – FURTHER DEVELOPMENTS | 357 | ||
18.4 REFERENCES | 357 | ||
Chapter 19: The Pearl® and WASSTRIP® processes (Canada) | 359 | ||
19.1 INTRODUCTION | 359 | ||
19.2 THE PROCESS | 360 | ||
19.2.1 The Pearl process description | 360 | ||
19.2.2 The WASSTRIP process description | 361 | ||
19.2.3 Crystal Green | 361 | ||
19.2.4 Key figures of the process | 362 | ||
19.3 OUTLOOK – FURTHER DEVELOPMENTS | 365 | ||
Chapter 20: The PHOSNIX process at the WWTP Lake Shinji East (Japan) | 367 | ||
20.1 INTRODUCTION | 367 | ||
20.2 PROCESS | 368 | ||
20.2.1 Apparatus | 368 | ||
20.2.2 Operation | 369 | ||
20.2.2.1 Main flow | 369 | ||
20.2.2.2 Struvite extraction | 369 | ||
20.3 COMMERCIAL PLANT | 369 | ||
20.3.1 Capacity | 369 | ||
20.3.2 Performance | 370 | ||
20.3.3 Cost | 370 | ||
20.3.4 Product quality | 371 | ||
20.4 APPLICATION FOR ANOTHER PURPOSE | 372 | ||
20.5 REFERENCES | 373 | ||
Chapter 21: The Stuttgart Process (Germany) | 375 | ||
21.1 INTRODUCTION | 375 | ||
21.2 THE PROCESS | 376 | ||
21.3 NUTRIENT RECOVERY PILOT PLANT | 377 | ||
21.3.1 Operation of the plant (batch mode) | 378 | ||
21.3.1.1 Acidic leaching of phosphate | 378 | ||
21.3.1.2 Dewatering of acidified digested sludge | 379 | ||
21.3.1.3 Struvite precipitation | 379 | ||
21.3.1.4 Recyclate/struvite harvesting | 381 | ||
21.3.2 Performance data | 382 | ||
21.3.2.1 Phosphorus recovery rates and recyclate yields | 382 | ||
21.3.2.2 Consumption of chemicals | 383 | ||
21.3.3 Recyclate quality | 384 | ||
21.3.3.1 Nutrients | 384 | ||
21.3.3.2 Metals | 384 | ||
21.3.3.3 Recalcitrant organic compounds (ROCs) | 388 | ||
21.3.4 Cost analysis | 388 | ||
21.4 KEY FIGURES OF THE PROCESS | 390 | ||
21.5 OUTLOOK – FURTHER DEVELOPMENTS | 390 | ||
21.6 REFERENCES | 390 | ||
Chapter 22: The ExtraPhos® process (Germany) | 391 | ||
22.1 INTRODUCTION | 391 | ||
22.2 THE PROCESS | 392 | ||
22.2.1 Description | 392 | ||
22.2.2 Key figures of the process | 393 | ||
22.3 OUTLOOK – FURTHER DEVELOPMENTS | 393 | ||
22.4 REFERENCES | 394 | ||
Chapter 23: KRN-Mephrec (Germany) | 395 | ||
23.1 INTRODUCTION | 395 | ||
23.2 THE PROCESS | 396 | ||
23.2.1 Description | 396 | ||
23.2.2 Key figures of the process | 399 | ||
23.3 OUTLOOK – FURTHER DEVELOPMENTS | 400 | ||
Chapter 24: The REMONDIS TetraPhos® Process at the WWTP in Hamburg (Germany) | 401 | ||
24.1 INTRODUCTION | 401 | ||
24.2 PHOSPHORUS RECOVERY: NOW & IN THE NEAR FUTURE | 402 | ||
24.2.1 Raw phosphates for industrial business | 402 | ||
24.2.2 Solubility of phosphates in ashes | 403 | ||
24.3 REMONDIS TETRAPHOS® PROCESS | 404 | ||
24.4 THE PILOT PLANT: PUTTING THEORY INTO PRACTICE | 406 | ||
24.4.1 Results: Phosphorus recovery & heavy metals | 407 | ||
24.5 OUTLOOK – UPSCALING TECHNOLOGY | 409 | ||
24.6 REFERENCES | 409 | ||
Chapter 25: The LeachPhos process at the waste-to-energy plant Bern (Switzerland) | 411 | ||
25.1 INTRODUCTION | 411 | ||
25.2 PROCESS DESCRIPTION | 412 | ||
25.2.1 Leaching process | 413 | ||
25.2.2 Precipitation process | 413 | ||
25.2.3 Wastewater treatment | 414 | ||
25.2.4 Equipment | 414 | ||
25.3 MASS BALANCE | 414 | ||
25.4 CONCLUSION | 414 | ||
25.5 REFERENCES | 416 | ||
Chapter 26: The PARFORCE-Technology (Germany) | 417 | ||
26.1 INTRODUCTION | 417 | ||
26.2 THE PROCESS | 418 | ||
26.2.1 Description | 418 | ||
26.2.2 Key figures of the process | 420 | ||
26.3 OUTLOOK – FURTHER DEVELOPMENTS | 424 | ||
26.4 REFERENCES | 424 | ||
Chapter 27: The AshDec® process – evolution from its earlier stages to current practice | 425 | ||
27.1 INTRODUCTION | 425 | ||
27.2 THE EVOLUTION | 426 | ||
27.2.1 Challenges and responses | 426 | ||
27.2.2 Towards the current AshDec® process | 428 | ||
27.3 KEY PROCESS FIGURES | 429 | ||
27.3.1 General data | 429 | ||
27.3.2 Utilities and consumables | 429 | ||
27.3.3 Waste | 429 | ||
27.3.4 Advantages | 430 | ||
27.4 THE PRODUCT | 430 | ||
27.5 OUTLOOK – DEVELOPMENT OPTIONS | 431 | ||
27.6 REFERENCES | 433 | ||
Chapter 28: Sludge melting system | 435 | ||
28.1 INTRODUCTION | 435 | ||
28.2 PROCESS DESCRIPTION | 436 | ||
28.2.1 Principle of phosphorus recovery | 436 | ||
28.2.2 Reactor | 437 | ||
28.2.3 Sewage sludge treatment process | 438 | ||
28.3 RESULTS OF THE LARGE-SCALE IMPLEMENTATION | 438 | ||
28.3.1 Pilot plant test | 438 | ||
28.3.2 Plant cultivation test | 441 | ||
28.4 COSTS | 441 | ||
28.5 CONCLUSION | 441 | ||
Chapter 29: The RecoPhos/Inducarb process (the Netherlands) | 443 | ||
29.1 INTRODUCTION | 443 | ||
29.2 THE PROCESS | 444 | ||
29.2.1 Description | 444 | ||
29.2.2 Key figures of the process | 445 | ||
29.3 OUTLOOK – FURTHER DEVELOPMENTS | 446 | ||
29.4 REFERENCES | 446 | ||
Chapter 30: Total phosphorus recovery and direct utilization of the sewage sludge ash as a fertilizer at Ulm WWTP (Germany) | 447 | ||
30.1 INTRODUCTION | 447 | ||
30.2 PROCESS DESCRIPTION | 449 | ||
30.3 PERFORMANCE DATA | 450 | ||
30.4 COSTS | 452 | ||
30.5 CONCLUSIONS | 452 | ||
30.6 REFERENCES | 453 | ||
Part IIIc: Phosphorus Recovery: Assessment | 455 | ||
Chapter 31: Comparison of technologies for phosphorus recovery – Identification of an ideal solution? | 457 | ||
31.1 INTRODUCTION | 457 | ||
31.2 OVERVIEW OF EXISTING TECHNOLOGIES | 458 | ||
31.2.1 Urine separation | 458 | ||
31.2.1.1 Process description | 458 | ||
31.2.1.2 Status of development | 459 | ||
31.2.2 Recovery from secondary treated effluent | 459 | ||
31.2.2.1 Process description | 459 | ||
31.2.2.2 Status of development | 460 | ||
31.2.3 Recovery from liquid phase of sludge treatment | 460 | ||
31.2.3.1 Process description | 460 | ||
31.2.3.2 Status of development | 460 | ||
31.2.4 Recovery from sewage sludge | 461 | ||
31.2.4.1 Process description | 461 | ||
31.2.4.2 Status of development | 462 | ||
31.2.5 Recovery from sewage sludge ashes | 463 | ||
31.2.5.1 Process description | 463 | ||
31.2.5.2 Status of development | 465 | ||
31.3 MATERIALS AND METHODS FOR THE COMPARATIVE ASSESSMENT | 466 | ||
31.3.1 Modular reference system and assessed technologies | 466 | ||
31.3.2 Recovery potential and assessment of the recovered materials | 467 | ||
31.3.3 Economic assessment | 467 | ||
31.3.3.1 Cost calculation | 467 | ||
31.3.3.2 Calculation of savings and revenues | 468 | ||
31.3.4 Environmental assessment | 468 | ||
31.4 RESULTS OF THE COMPARATIVE ASSESSMENT | 469 | ||
31.4.1 Recovery potential and assessment of the recovered materials | 469 | ||
31.4.1.1 Recovery potential | 469 | ||
31.4.1.2 Nutrient content and plant availability | 469 | ||
31.4.1.3 Pollutants content | 471 | ||
31.4.1.4 Texture and handling | 472 | ||
31.4.2 Economic assessment | 474 | ||
31.4.3 Environmental assessment | 476 | ||
31.4.3.1 Cumulative energy demand (CED) | 476 | ||
31.4.3.2 Gaseous emissions (CO2e) with global warming potential (GWP) | 476 | ||
31.4.3.3 Gaseous emissions (SO2e) with acidification potential (AP) | 477 | ||
31.4.3.4 Relevance of the environmental impact in the context of the status quo | 479 | ||
31.4.4 Uncertainty | 480 | ||
31.5 CONCLUSIONS | 481 | ||
31.6 REFERENCES | 483 | ||
Chapter 32: Success factors for implementing P recovery and recycling technologies | 487 | ||
32.1 INTRODUCTION | 487 | ||
32.1.1 The value chain | 487 | ||
32.1.2 Success factors | 489 | ||
32.2 TECHNOLOGIES UNDER DEVELOPMENT, IN USE, OR BEING IMPLEMENTED | 496 | ||
32.2.1 Sewage sludge in direct application | 496 | ||
32.2.2 Struvite recovery | 496 | ||
32.2.3 Sludge processes | 499 | ||
32.2.3.1 EXTRAPHOS by Budenheim | 499 | ||
32.2.3.2 Acidic leaching of digested sludge | 500 | ||
32.2.4 Ash based processes | 501 | ||
32.2.4.1 Glatt® Seraplant | 502 | ||
32.2.4.2 Ecophos | 503 | ||
32.2.4.3 LeachPhos | 504 | ||
32.2.4.4 TetraPhos | 505 | ||
32.2.4.5 AshDec | 505 | ||
32.2.4.6 Mephrec | 506 | ||
32.2.4.7 Recophos-P4 | 507 | ||
32.3 CONCLUSIONS | 508 | ||
32.4 ADDITIONAL CONSIDERATIONS | 510 | ||
32.5 OUTLOOK | 511 | ||
32.6 REFERENCES | 512 | ||
Chapter 33: Phosphorus recovery – decision-making under uncertainties, sector integration and digital modernization by using multi-criterial decision analysis | 515 | ||
33.1 INTRODUCTION | 515 | ||
33.2 DEFINING THE MATTER AT HAND | 516 | ||
33.3 THE INNOVATION FIELD FOR PHOSPHORUS RECOVERY | 517 | ||
33.3.1 Imperative of phosphorus recovery | 518 | ||
33.3.2 General framework conditions for the modernization of WWTPs | 519 | ||
33.3.3 Criteria for comparing approaches towards modernization of WWTPs | 521 | ||
33.4 SOCIOLOGICAL METHODS FOR TECHNOLOGICAL INNOVATIONS IN THE WASTEWATER SECTOR | 523 | ||
33.5 SUMMARY AND PERSPECTIVE | 530 | ||
33.6 REFERENCES | 532 | ||
Part IV: Outlook | 535 | ||
Chapter 34: Wastewater treatment of the future: Health, water and resource protection | 537 | ||
34.1 INTRODUCTION | 537 | ||
34.2 OBJECTIVES OF WASTEWATER TREATMENT | 538 | ||
34.2.1 Health protection | 538 | ||
34.2.1.1 Safeguarding basic sanitation | 538 | ||
34.2.1.2 Disinfection: Bathing water quality and water reuse | 539 | ||
34.2.2 Water protection | 540 | ||
34.2.2.1 European water framework directive | 540 | ||
34.2.2.2 Minimization of nutrient input into waterbodies | 540 | ||
34.2.2.3 Micropollutants, nanoparticles and microplastics | 541 | ||
34.2.2.4 Substance prohibition for water (and health) protection | 541 | ||
34.2.3 Resource protection | 541 | ||
34.3 RESOURCES IN WASTEWATER: WATER, NUTRIENTS AND ENERGY | 542 | ||
34.3.1 Water | 542 | ||
34.3.2 Nutrients | 542 | ||
34.3.3 Energy | 544 | ||
34.3.3.1 Chemically bound energy in wastewater: Evaluation via COD balancing | 544 | ||
34.3.3.2 Sewage sludge treatment plants in interaction with the energy industry | 545 | ||
34.4 WASTEWATER TREATMENT PLANTS OF THE FUTURE: FROM TREATMENT PLANT TO (SYSTEM) SERVICE PROVIDER | 547 | ||
34.5 CONCLUSION AND OUTLOOK: FROM TREATMENT FACILITY TO SYSTEM SERVICE PROVIDER | 549 | ||
34.6 REFERENCES | 550 | ||
Index | 555 |