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BS 10: Wet Bulk Solids Storage

BS 10: Storage of Wet Bulk Solids
     Part 1: Storage Options for Wet Bulk Solids
         1. INTRODUCTION
             1.1 Scope of Review
             1.2 Requirements of a Storage System
         2. BASIC MATERIAL PROPERTIES
             2.1 Wall Friction and Adhesion
             2.2 Internal Shear Strength
             2.3 Phase Separation
             2.4 Particle Size Segregation
             2.5 Ageing Effects
         3. NON SETTLING PASTES AND CAKES
             3.1 Stockpiles
                 3.1.1 Use of Stockpiles
                 3.1.2 Special Considerations for Wet Solids
                 3.1.3 Conclusions
             3.2 Hoppers, Silos, Bins
                 3.2.1 Available Design Methods
                 3.2.2 Design Requirements for Wet Solids
                 3.2.3 Discharge Aids for Wet Solids
                 3.2.4 Conclusions
         4. NOTATION
         5. REFERENCES
         6. APPENDIX A. A CLASSIFICATION OF ROUGHNESS OF INTERAL WALLS
     Part 2: Design of Hoppers, Silos, Bins and Bunkers
         SUMMARY
         1. INTRODUCTION
             1.1 Scope of guide
             1.2 Identification of materials to be considered as wet or damp bulk solids
             1.3 Mass flow and core flow discharge patterns, and their respective advantages
                 1.3.1 Mass flow and core flow
                 1.3.2 The need for mass flow with wet materials
             1.4 Operational failures: arching, "rat-holing", etc.
             1.5 Fundamental principles of design for reliable flow from hoppers, bins, bunkers and silos
                 1.5.1 Flow down the walls; the critical angle for mass flow
                 1.5.2 The arch, stresses and failure
                 1.5.3 Critical outlet dimension for a hopper
                 1.5.4 Summary of critical dimensions
         2. BULK SOLID FLOW TESTING
             2.1 The need to predict mass flow angle, and outlet dimension to prevent arching
             2.2 Measurement of internal flow properties
                 2.2.1 Explanation of the strength of a bulk solid
                 2.2.2 Determination of flow function FF by shear testing
                 2.2.3 Selection and preparation of test specimens
                 2.2.4 Shear testers
                 2.2.5 The Jenike shear tester
                 2.2.6 The Walker shear tester
                 2.2.7 The Johansen indicisers
             2.3 Time consolidation effects
                 2.3.1 The need to account for time consolidation
                 2.3.2 Measurement of strength under time consolidation
                 2.3.3 A short cut to save some time
             2.4 Measurement of wall friction properties
             2.5 Density and compressibility test
             2.6 Special problems with wet materials
                 2.6.1 Expression of liquid in testing
                 2.6.2 Variation in moisture content on the plant
                 2.6.3 Change in moisture content during testing, and/or during storage
             2.7 Caking effects
         3. DESIGN OF THE CONVERGING SECTION OF THE VESSEL
             3.1 Introduction
             3.2 Hopper shapes
             3.3 Outlet size and wall angle
                 3.3.1 Jenike "Flow - no-flow" criterion
                 3.3.2 Flow functions and flow factors
                 3.3.3 Outlet dimension and wall angle
                 3.3.4 Period of storage and time consolidation effects
                 3.3.5 Designing for time consolidation
                 3.3.6 Practical ways of minimising time consolidation
                 3.3.7 The effect of variation in moisture content
                 3.3.8 What to do if no hopper design is possible
             3.4 Advantages of certain hopper shapes
                 3.4.1 Headroom and capacity
                 3.4.2 Tolerance of variation in bulk solid flow characteristics
                 3.4.3 High wall friction
                 3.4.4 Summary of the advantages of plane flow
                 3.4.5 Parallel sided bins with full live bottoms
             3.5 Use of special wall materials including "low friction" linings
                 3.5.1 Materials available
                 3.5.2 Choosing between low friction wall materials
             3.6 Need for air injection
             3.7 Core flow design
             3.8 Overcoming space limitations
         4. CASE STUDIES OF BIN DESIGNS
             4.1 Introduction
             4.2 Moist Fine Chemical Powder
                 4.2.1 Wall materials considered
                 4.2.2 Interpretation of shear loci
                 4.2.3 Production of Failure Function FF, and other test results
                 4.2.4 Determination of hopper dimensions
             4.3 Wet pharmaceutical powder
             4.4 Oat meal
             4.5 Wet pharmaceutical intermediate
             4.6 Wall friction with wet desulphogypsum
             4.7 Summary of calculated results
             4.8 Note on all graphs and extrapolation
         5. FEEDERS AND DISCHARGE AIDS
             5.1 Distinction between feeders and discharge aids
             5.2 Feeder types and advantages
                 5.2.1 Introduction
                 5.2.2 Belt feeders
                 5.2.3 Apron feeders and rotary feeders
                 5.2.4 Rotary table feeders
                 5.2.5 Screw feeders
                 5.2.6 Vibratory feeders
                 5.2.7 En-masse feeders
             5.3 Feeders for full-live-bottom bins or very large outlets
                 5.3.1 Belt, apron, en-masse, rotary table and vibratory feeders
                 5.3.2 Multiple screw feeders
                 5.3.3 Orbiting screws or "sweep augers"
                 5.3.4 The Redler "Circular Bin Discharger"
                 5.3.5 The Saxlund moving-floor discharger
             5.4 General notes about selection and installation of feeders
             5.5 Discharge aids
                 5.5.1 Manual versus automatic methods
                 5.5.2 Pneumatic methods
                 5.5.3 Vibrational methods
                 5.5.4 Mechanical methods
                 5.5.5 Concluding remarks on selection of discharge aids
         6. CAKING OF BULK SOLIDS
             6.1 Introduction
             6.2 Identification of caking
             6.3 Types of caking
             6.4 Materials affected, and occasions of occurrence
             6.5 The mechanism of moisture migration caking
             6.6 Elimination of caking by conditioning
                 6.6.1 Conditioning of the product
                 6.6.2 Conditioning equipment
                 6.6.3 Determination of conditioning requirement
                 6.6.4 Design of conditioning equipment for the plant
             6.7 Control of caking by reducing temperature gradients
             6.8 Reducing caking by means of "flow additives"
             6.9 "Crusting" resulting from moist air in silo head space
             6.10 Summary
         7. CONTROL AND MEASUREMENT OF DISCHARGE RATES
             7.1 Hopper discharge rate limitations
             7.2 Effects of feeder size
             7.3 Controlling rates of discharge from feeders, and drive characteristics
             7.4 Measurement of discharge rates from hoppers
                 7.4.1 Belt weighing
                 7.4.2 Loss-in-weight feeding
                 7.4.3 Batch weighing
                 7.4.4 Other methods
         8. PREDICTION OF STRESSES IN HOPPERS
             8.1 General
             8.2 Procedures for structural design
             8.3 Predicting silo loadings
             8.4 Special problems presented by wet materials
                 8.4.1 Expression of liquid (draining)
                 8.4.2 Liquefaction
             8.5 Avoiding Problems With Existing Structures
         9. DIGEST OF THE DESIGN PROCESS FOR HOPPERS
         10. TROUBLESHOOTING OF HOPPERS WHICH DO NOT WORK PROPERLY
             10.1 Hoppers which do not discharge properly
             10.2 Hoppers which discharge material of variable quality
         11. CONCLUSIONS AND GENERAL OBSERVATIONS
         12. REFERENCES
         13. ACKNOWLEDGEMENTS
         14. NOMENCLATURE USED IN THIS DOCUMENT

Volume BSH 10: Part 1 Survey of Storage Options for Bulk Solids

This part discusses the design of hoppers, bins, silos or bunkers for wet, granular solids. Such material will generally be unsaturated, i.e., the material will be a three-phase mixture of granular solids, water (or other liquid) and occluded air (or other gas).


Volume BSH 10: Part 2 Design Guide for Storage of Wet Bulk Solids in Hoppers, Silos, Bins and Bunkers

This part is a design guide intended to be used as a reference work for the design of hoppers, silos, bins and bunkers for the storage and discharge of wet bulk solids. The majority of the part refers to the design of the discharging section of the storage vessel, since it is this that is the key to proper function of a vessel. In practice, this means principally the selection of the hopper angle to obtain the correct flow pattern, and the outlet to ensure that the material will not arch over it. It also includes the correct selection of the wall material for the converging section, together with selection and interfacing of the feeder to draw material out of the bottom of the hopper.

The part concentrates on practical considerations and the methods of design, and how to avoid practical pitfalls, rather than fundamental analysis and theory. However, some explanation of fundamental concepts has been included to enable a practical engineer to obtain an outline understanding of the reasons behind the steps laid down. References are included for the use of those seeking a more rigorous fundamental understanding. Case studies are included to illustrate the design techniques described.

The part includes "digests" of the approaches to be used when designing and troubleshooting bins for wet materials. The reader is particularly encouraged to use and refer to these when trying to use the part, as they lay out a structured approach to the processes of design and troubleshooting. Finally the part incorporates a section describing the processes of "caking" in wet materials and how this can be avoided.

The part has been written to be particularly relevant to bulk solids which include sufficient liquid (of any type) to modify significantly their flow characteristics from those of dry materials, but are not so wet as to be better characterised by rheological techniques. Essentially this means that compared with dry materials, they have significant cohesive strengths, ie., they are not "free-flowing", and significant time consolidation characteristics, ie., if left in a hopper they gain strength markedly and become more difficult to discharge. Some dry materials exhibit these characteristics, and the guidance in this work is equally relevant to the design of hoppers for those materials. Note that materials which have moisture contents well above the level at which draining begins, should be treated as non-Newtonian liquids, using rheological techniques. Such materials are beyond the scope of this part (see the Slurry Handling Knowledge Base).