| Preface |
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| 1 Solid/liquid separation equipment |
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1.1 Gravity thickeners and clarifiers |
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1.1.1 Circular basin thickener |
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1.1.2 High capacity thickeners |
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1.2.1 Conical reverse flow |
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1.3.1 Sedimenting centrifuges |
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1.3.2 Filtering centrifuges |
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1.3.2.5 Inverting bag centrifuge |
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1.4.1.2 Multi-element leaf |
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1.4.1.4 Horizontal rotary |
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1.4.2 Pressure filters and presses |
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1.4.2.2 Multi-element leaf or candle |
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1.4.2.5 Variable volume filters and Presses |
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1.4.2.6 Continuous pressure filters |
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1.4.3.1 Precoat rotary drum |
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1.6.2 Low shear crossflow |
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1.6.3 High shear crossflow |
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1.7.3 Gravity Nutsche filters |
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1.7.4 Gravity belt filter |
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1.8 Force field assisted separations |
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1.8.2 High voltage electric field |
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1.8.3 Low voltage electric field |
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| 2 Filter media |
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2.1 Properties of filter media |
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2.2.1.2 Fabric constructions and properties |
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2.2.1.3 Fabric finishing processes |
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2.2.2.1 Surface coated fabrics |
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2.2.2.2 Laminated fabrics |
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2.2.2.3 Double layer weaves |
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2.2.3 Needlefelts and other nonwoven media |
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2.2.4 Selection and applications of filter cloths |
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2.2.5 Damage to filter media |
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2.3 Filter papers and sheets |
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2.3.1.1 Industrial papers |
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2.3.1.2 Laboratory papers |
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2.6 Porous sheets and tubes |
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2.8 Precoats and body aids (filter aids) |
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| 3 Pretreatment of suspensions |
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3.2 Coagulation principles and mechanisms |
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3.2.1 Mechanical agitation |
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3.2.2 Indifferent electrolytes |
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3.2.3 Multivalent metal ions (inorganic coagulants) |
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3.2.4 Lower molecular weight polymers (organic coagulants) |
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3.3 Flocculation principles and mechanisms |
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3.3.1 Forms of flocculation and polymer adsorption |
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3.3.2 Lower molecular weight polymers (charge neutralisation) |
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3.3.3 Higher molecular weight polymers (bridging flocculation) |
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3.4 Types of pretreatment chemicals |
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3.5 Effectiveness and selection of chemical pretreatments |
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3.5.3 Capillary suction test |
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3.5.4 Coagulant and flocculant selection |
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3.6 Other methods of pretreatment |
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3.6.2 Suspension freezing |
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3.6.3 Particle/crystal formation |
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3.6.4 Elutriation and suspension thickening |
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3.6.7 Addition of solvents/surfactants |
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3.6.8 Addition of filter aid |
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| 4 Data acquisition, analysis and scale-up |
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4.1 Filtration (cake formation) |
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4.1.2 General filtration equation |
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4.1.3 Evaluation of terms in the general filtration equation |
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4.1.4 Evaluation of filter cake properties |
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4.2.2 Data analysis procedure |
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4.3.2 Data analysis procedure |
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4.4.2 Data analysis procedure |
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4.5 Expression (cake formation/consolidation) |
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4.5.1 General test procedure |
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4.5.3 Filtration phase analysis |
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4.5.4 Consolidation phase analysis |
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4.5.6 Estimates of the transition point and consolidation index |
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4.6 State-of-the-art apparatus |
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4.7 Evaluation of scale-up coefficients |
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| 5 Selection, data analysis and simulation by computer software |
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5.1.1 Methods of equipment selection |
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5.1.2 Recommended selection procedure |
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5.1.2.1 Specification of duty |
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5.1.2.2 Specification of sedimentation performance |
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5.1.2.3 Specification of filtration performance |
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5.1.2.4 Tables of equipment and letter codings |
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5.2 Implementation of computer software |
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5.3.1 Equipment selection module |
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5.3.2 Data analysis module |
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5.3.3 Equipment simulation modules |
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5.4.1 Example 5.1: Basic selection and data analysis procedures |
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5.4.2 Example 5.2: Advanced selection procedure |
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5.5 Shortlisting equipment for pilot scale testing and/or simulation |
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| 6 Process design for batch separations |
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6.1 Batch filter cycle configurations |
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6.1.2 Multi-element vacuum filter |
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6.1.3 Multi-element leaf and candle pressure filters |
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6.1.4 Horizontal diaphragm, plate and frame, and recessed plate presses |
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6.1.5 Vertical diaphragm presses |
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6.2 Design equations for batch filter cycles |
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6.2.1 Filtration (cake formation) phase |
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6.2.1.1 Nutsche and multi-element vacuum filters |
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6.2.1.2 Filter and diaphragm presses and multi-element leaf pressure filters |
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6.2.1.4 Multi-element candle filter |
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6.2.2 Compression deliquoring |
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6.2.3 Displacement washing |
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6.2.5 Optimisation of filtration time for batch filters |
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6.3 Design equations for centrifugal filter cycles |
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6.4 Examples of batch filter cycle calculations |
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6.4.1 Example 6.1: Horizontal diaphragm filter press |
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6.4.1.1 Cake formation (filtration) phases |
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6.4.1.2 Consolidation (compression deliquoring) phase |
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6.4.1.4 Gas deliquoring phase |
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6.4.1.5 Summary of results and filter cycle illustrations |
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6.4.2 Example 6.2: Nutsche filter |
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6.4.2.1 Cake formation (filtration) phase |
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6.4.2.3 Gas deliquoring phase |
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6.4.2.4 Summary of results and process implications |
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6.5 Example of computer simulation – diaphragm filter press |
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6.5.1 Fixed mass of solids |
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| 7 Process design for continuous separations |
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7.1 Continuous filter cycle configurations |
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7.1.1 Horizontal belt filter |
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7.1.3 Rotary table and tilting pan filters |
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7.2 Design equations for continuous filter cycles |
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7.2.1 Filtration (cake formation) phase |
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7.2.2 Displacement washing |
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7.3 Examples of continuous filter cycle calculations |
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7.3.1 Example 7.1: Horizontal belt filter |
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7.3.1.1 Cake formation (filtration) phase |
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7.3.1.3 Deliquoring phase |
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7.3.1.4 Summary of results and filter cycle illustrations |
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7.3.2 Example 7.2: Rotary drum filter |
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7.3.2.1 Cake formation (filtration) phase |
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7.3.2.4 Deliquoring phase |
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7.3.2.5 Summary of results and filter cycle illustrations |
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7.4 Example of computer simulation — belt filter |
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7.4.1 Effects of belt speed |
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7.4.2 Effects of applied vacuum |
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7.4.3 Effects of plant altitude (barometric pressure) |
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7.4.4 Effects of temperature |
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7.4.5 Effects of particle size |
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| Nomenclature |
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| Bibliography |
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| Appendix A: Variable ranges for filter cycle calculations |
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| Appendix B: Correlations for cake washing and gas deliquoring |
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| Appendix C: Definitions and conversions for concentration |
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| Appendix D: Troubleshooting filter operation |
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| Appendix E: Comparisons between experimental data and design equation predictions |
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| Index |
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