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Aerobic Granule Reactor Technology

Aerobic Granule Reactor Technology

M. K. de Kreuk | L. M. M. de Bruin

(2004)

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Book Details

Abstract

A new development for the treatment of domestic wastewater is a technology based on aerobic granular sludge. Granular sludge can be developed under specific process conditions. Because of the unique properties of this granular sludge, high volumetric loading rates of aeration tanks can be applied. Thanks to excellent settling properties, the separation of treated wastewater and granular sludge can take place at high hydraulic loading rates. Depending on the chosen process configuration good effluent quality can be obtained, complying with the stringent effluent requirements regarding nitrogen and phosphorus, which can be expected in the future. In this way aerobic granular sludge has the potential to contribute significantly to wastewater treatment management. This report describes the results of research carried out at the Technical University of Delft.

Table of Contents

Section Title Page Action Price
TABLE OF CONTENTS 1
PREFACE vii
SUMMARY viii
1.0 INTRODUCTION xi
History of the project xi
Objectives xii
2.0 METHODS xiii
Reactor set-up xiii
Operational procedures xiii
Control xiv
Analytical procedures xiv
3.0 INFLUENCE OF FEEDING TIME xvi
3.1 Introduction xvi
3.2 Bottleneck of scale-up xvii
3.3 Results xvii
3.3.1 Granulation xvii
3.3.2 Conversion Processes xviii
3.4 Conclusions xx
4.0 INFLUENCE OF THE DISSOLVED OXYGEN CONCENTRATION xxi
4.1 Introduction xxi
4.2 Low DO and pulse feed xxi
4.2.1 Granulation xxi
4.2.2 Conversion processes xxiii
4.3 Low DO and long anaerobic feeding xxiii
4.3.1 Granulation xxiii
4.3.2 Conversion processes xxiv
4.4 Conclusions xxv
5.0 INFLUENCE OF THE REACTOR CONFIGURATION xxvii
5.1 Introduction xxvii
5.2 Results xxvii
5.2.1 Granulation xxvii
5.2.2 Conversion processes xxviii
5.3 Conclusion xxviii
6.0 EXPERIMENT WITH PRE-TREATED SEWAGE xxix
6.1 Introduction xxix
6.2 Selection of the influent xxix
6.2.1 Pre-treatment xxix
6.2.2 Selection of the raw sewage xxix
6.3 Results xxx
6.3.1 Granulation xxx
6.3.2 Conversion processes xxxii
6.4 Conclusions xxxiii
7.0 DESIGN AND ECONOMICS OF A FULL-SCALE GSBR TREATMENT PLANT xxxiv
7.1 Introduction xxxiv
7.2 General basic conditions xxxiv
7.2.1 Capacity and wastewater composition xxxiv
7.2.2 Effluent requirements xxxv
7.2.3 Flow pattern xxxv
7.2.4 Cost estimates xxxvi
7.2.5 Footprint and land price xxxvi
7.3 Reference systems xxxvi
7.3.1 Introduction xxxvi
7.3.2 Design assumptions xxxvii
7.3.3 Dimensions and costs xxxvii
7.4 Interaction between feasibility study and research xxxix
7.5 Design GSBR xl
7.5.1 Assumptions xl
7.5.2 Buffer capacity xlii
7.5.3 Design outline xlii
7.5.4 Effluent quality xlii
7.5.5 Costs xliii
7.6 Sensitivity analysis xliv
7.6.1 RWF/DWF ratio xliv
7.6.2 Land price xlv
7.6.3 Post treatment alternatives xlv
7.6.4 Round or rectangular? xlv
7.6.5 Cycle time xlvi
7.7 Conclusions and potential xlvi
7.7.1 Reference alternatives xlvi
7.7.2 GSBR xlvi
8.0 CONCLUSIONS AND RECOMMENDATIONS xlviii
9.0 SYMBOLS AND ABBREVIATIONS l
10.0 LITERATURE li
APPENDIX 1 liii
PFDS REFERENCE SYSTEMS liv
APPENDIX 2 lv
PFDS GSBR ALTERNATIVES lvi
APPENDIX 3 lvi
DESIGN AND COSTS OF REFERENCE 1 lviii
APPENDIX 4 lvii
DESIGN AND COSTS OF REFERENCE 2 lviii
APPENDIX 5 lviii
DESIGN AND COSTS OF REFERENCE 3 lix
APPENDIX 6 lix
DESIGN AND COSTS GSBR WITH POST TREATMENT AND BIO-P lx
APPENDIX 7 lx