Acknowledgements |
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1 Background, problem statement and outline |
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1 | (6) |
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1.1 Introduction & study background |
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1 | (1) |
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1.2 State-of-the-art in residuals processing |
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2 | (1) |
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1.3 Problem statement and hypothesis |
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2 | (1) |
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1.4 Overview and scope of study |
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3 | (1) |
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1.5 Outline and structure of the thesis |
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4 | (3) |
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2 Fundamentals of flocculation and colloidal stability |
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7 | (16) |
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2.1 Structure formation in dispersed systems |
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7 | (1) |
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2.2 Colloidal stability and interfacial forces |
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8 | (1) |
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2.3 Kinetics of fine particle aggregation |
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9 | (12) |
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2.3.1 Perikinetic particle aggregation |
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11 | (1) |
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2.3.2 Hydrodynamic-mediated interactions |
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11 | (1) |
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2.3.2.1 Classical orthokinetic aggregation |
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11 | (2) |
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2.3.2.1 Particles in laminar shear |
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13 | (1) |
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2.3.2.1 Particles in turbulent shear |
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13 | (1) |
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2.3.3 Extended orthokinetic flocculation |
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14 | (1) |
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2.3.3.1 Mechanisms of pelleting flocculation |
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15 | (1) |
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2.3.3.2 Pelleting reactor systems |
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16 | (1) |
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2.3.3.2 Annular-based reactors |
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16 | (1) |
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2.3.3.2 Sludge blanket clarifiers |
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16 | (1) |
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2.3.3.3 Structure and morphology of pellet floes |
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17 | (2) |
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2.3.4 Polymer-mediated interactions |
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19 | (1) |
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2.3.4.1 Charge neutralization |
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20 | (1) |
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20 | (1) |
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2.3.4.3 Charge-patch formation |
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21 | (1) |
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2.4 Flocculation assessment techniques |
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21 | (2) |
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3 Hydrodynamics and floe stability in sheared systems |
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23 | (12) |
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3.1 Hydrodynamics and fluid-particle interactions |
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23 | (3) |
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3.1.1 Fluid mixing and particle dispersion |
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23 | (1) |
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3.1.2 Micro, meso, and macro mixing |
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24 | (1) |
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3.1.3 Characterization of fluid-particle mixing |
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25 | (1) |
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3.2 Turbulent aggregation processes |
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26 | (9) |
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3.2.1 Energy dissipation in turbulent flow |
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26 | (1) |
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3.2.2 Agglomerate strength and hydrodynamic stress |
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27 | (2) |
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3.2.3 Fluid-particle interactions and floe stability |
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29 | (4) |
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3.2.4 Mechanisms of aggregate disruption |
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33 | (2) |
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4 Materials and experimental methods |
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35 | (12) |
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35 | (6) |
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35 | (1) |
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4.1.2 Ferric hydroxide slurry |
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35 | (1) |
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35 | (2) |
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37 | (2) |
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4.1.5 Batch vortex reactor |
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39 | (1) |
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4.1.6 Continuous vortex reactor |
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40 | (1) |
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4.1.7 Gravity dewatering chamber |
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41 | (1) |
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41 | (6) |
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4.2.1 Preparation of substrates and reagents |
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41 | (1) |
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4.2.2 Flocculation and sedimentation tests |
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42 | (1) |
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4.2.3 Surface charge measurements |
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42 | (1) |
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4.2.4 Characterization of the reactor supernatant |
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42 | (1) |
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4.2.5 Flow stream characterization |
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43 | (1) |
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4.2.6 Agglomerate preparation and characterization |
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44 | (3) |
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5 Design concept and process description |
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47 | (14) |
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5.1 Structure formation and hydrodynamic conditions |
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47 | (14) |
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5.1.1 Theoretical description of the agglomeration process |
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47 | (2) |
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5.1.2 Hydrodynamics and flow pattern in the flow units |
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49 | (1) |
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5.1.3 Experimental analysis of hydrodynamics and vortex pattern |
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50 | (1) |
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5.1.3.1 Description of the experimental setup and limitations |
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51 | (1) |
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5.1.3.2 Effect of agitation speed on the flow stream and vortex pattern |
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52 | (2) |
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5.1.3.3 Effect of reactor geometry on the flow stream and vortex pattern |
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54 | (1) |
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5.1.3.4 Description of the flow stream and vortex pattern along the rotor-stator cavity |
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54 | (2) |
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5.1.3.5 Process relevance of the flow conditions |
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56 | (5) |
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6 Mixing and hydrodynamic analysis |
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61 | (6) |
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6.1 Theoretical analysis of the flow conditions |
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61 | (1) |
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6.3 Fluid flow and mixing characteristics |
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61 | (3) |
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6.4 Micro and macro mixing |
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64 | (3) |
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7 Optimization of the micro processes |
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67 | (20) |
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7.1 Optimization of the physicochemical process |
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67 | (11) |
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7.1.1 Single and dual polymer conditioning |
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68 | (1) |
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7.1.2 Particle-polymer interaction and selection of optimum dose |
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69 | (1) |
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7.1.3 Polymer-dose response in single polymer treatment |
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70 | (2) |
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7.1.4 Polymer-dose response in dual-polymer additions |
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72 | (3) |
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7.1.5 Supernatant clarity at the optimum dosage |
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75 | (1) |
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7.1.6 Specific sediment volume at optimum dosage |
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76 | (1) |
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7.1.7 Process relevance of the physicochemical parameters |
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77 | (1) |
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7.2 Optimization of the pelleting process |
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78 | (6) |
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7.2.1 Effects of micro processes on the pelleting process |
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78 | (4) |
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7.2.2 Effect of optimum dose on the process efficiency |
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82 | (1) |
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7.2.3 Effects of micro processes on the solids fraction |
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82 | (1) |
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7.2.4 Predicted and effective polymer dose |
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83 | (1) |
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7.3 Process relevant pellet characteristics |
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84 | (3) |
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7.3.1 Image and particle size analysis |
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84 | (1) |
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7.3.2 Agglomerate strength analysis |
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85 | (2) |
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8 Conclusions and perspectives |
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87 | (4) |
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8.1 Effect of rotor-stator configuration |
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87 | (1) |
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8.2 Effect of process conditions |
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88 | (1) |
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88 | (1) |
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8.3.1 Effect of other process conditions |
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88 | (1) |
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8.3.2 Computational study of the fluid flow |
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89 | (1) |
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8.3.3 Numerical modeling of the pelleting process |
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89 | (1) |
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89 | (2) |
Appendix |
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91 | (16) |
References |
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107 | (14) |
List of publications |
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121 | |