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Slurry 7: Instrumentation

Slurry 7: Instrumentation
     Part 1: Level Measurement Techniques
         1. INTRODUCTION
         2. PRIMARY CONSIDERATIONS FOR INSTRUMENT SELECTION
         3. DESCRIPTION OF BASIC SENSOR SYSTEMS
             3.1 Float Level Sensors
                 3.1.1 Float Switches
                 3.1.2 Continuous Indicating and Multiple Switch Float Systems
             3.2 Displacer Type Level Sensors
                 3.2.1 Displacer Type Level Switches
                 3.2.2 Continuous Displacer Type Level Systems
             3.3 Capacitance Type Level Detectors
                 3.3.1 Capacitance Level Switches
                 3.3.2 Continuous Capacitance Level Systems
             3.4 Vibrating Reed or Tuning Fork Level Switch
             3.5 Ultrasonic Level Sensors
                 3.5.1 Damped Ultrasonic Level Switches
                 3.5.2 Transmission Ultrasonic Level Switches
                 3.5.3 Pulse Echo Continuous Ultrasonic Level Sensors
             3.6 Conductivity Level Switches
             3.7 Radiation Type Level Sensors
             3.8 Gas Bubblers
             3.9 Diaphragm Type Level Sensors
             3.10 Tape Type Level Gauges
                 3.10.1 Float Actuated Tape Level Gauges
                 3.10.2 Displacer Actuated Tape Level Gauge
                 3.10.3 Comments on Liquid Service Tape Gauges
                 3.10.4 Plumb Bob Level Gauges
             3.11 Pressure Level Detector Systems
                 3.11.1 Pressure Transducer Level Sensors
                 3.11.2 Differential Pressure Transducer Level Systems
             3.12 Rotating Paddle Level Switches
             3.13 Resistance Tape Level Detector
             3.14 Tilt Level Switches
             3.15 Thermal Level Switches
             3.16 Weighing Methods
             3.17 Optical Level Detection Systems
                 3.17.1 Optical Level Switches
                 3.17.2 Continuous Optical Level Sensors
             3.18 Microwave Level System
             3.19 Radio Frequency/Admittance Systems
             3.20 Radar Level Gauges
             3.21 Other Systems
         4. PROBLEM AREAS IN LEVEL MEASUREMENT
             4.1 Temperature of Vessel Environment
             4.2 Pressure of Vessel Environment
             4.3 Compatibility of Materials
             4.4 Boiling, Bubbling or Aerated Materials
             4.5 Foaming Liquids
             4.6 Stirred or Agitated Vessels
             4.7 Hard to Handle Materials
             4.8 Liquid/Liquid Interface Detection
             4.9 Variable Specific Gravity or Bulk Density
             4.10 Dusty Environment
             4.11 Angle of Repose of Solids
             4.12 Application in Hazardous Areas
         5. CONCLUSIONS
         6 APPENDIX A LEVEL MANUFACTURERS SOURCE ADDRESS LIST
         7 APPENDIX B LEVEL MEASURING TECHNIQUES AVAILABLE FROM GIVEN SOURCES
             Table B1 List of Level Measuring Techniques
             Table B2 Level Measuring Techniques Available from UK Sources
     Part 2: On-line Measurement of Viscosity
         1. INTRODUCTION
             1.1 Scope of Review
             1.2 Viscosity and other rheological properties
             1.3 Viscometers/rheometers for on-line measurement and control
             1.4 Types of on-line viscometers/rheometers
         2. COMMERCIAL VISCOMETERS
             2.1 Rotational viscometers
                 2.1.1 Coaxial cylinder viscometers
                 2.1.2 Rotating bob viscometer
                 2.1.3 Nutating cylinder viscometer
                 2.1.4 Parallel plate viscometer
                 2.1.5 Rotating disc viscometer
             2.2 Tube viscometers
                 2.2.1 Full bore pipe viscometers
                 2.2.2 Capillary tube viscometers
             2.3 Moving cylinder viscometers
             2.4 Drag on blade viscometers
             2.5 Moving blade viscometers
             2.6 Squeeze flow viscometers
             2.7 Vibrational viscometers
                 2.7.1 Description of commercially available instruments
                 2.7.2 Description of obsolete instruments
         3. COMMERCIAL RHEOMETERS
             3.1 Complex Dynamic Viscosity
             3.2 Normal Stress
         4. HOME-MADE INSTRUMENTS
             4.1 The BFMIRA In-Line Viscometer
             4.2 The Automatic On-Line Viscometric Technique Comprising the WSL Modified Rheomat 15 Viscometer
             4.3 WSL In-Line Oscillatory Viscometer
             4.4 UCL Continuous Rotational Viscometer
             4.5 FRS Immersion Viscometer
             4.6 Lyons In-line Consistency Meter for Measuring Bread Dough
             4.7 The Strain Gauge Method for Determining Viscosity
             4.8 Polysar Automatic Analyser incorporating the Ubbelohde Viscometer
             4.9 Continuous Flow Viscometer for Cell Suspension Viscosity
             4.10 Du Pont Continuous Pipeline Viscometer using Two Capillary System
             4.11 A Continuous Recording Bridge Viscometer
         5. FACTORS AFFECTING VISCOMETER SELECTION
             5.1 Material considerations
             5.2 Process operating conditions
                 5.2.1 Temperature
                 5.2.2 Pressure
                 5.2.3 Flow condition
             5.3 Viscometer operating range
                 5.3.1 Temperature
                 5.3.2 Pressure
                 5.3.3 Shear rate range
                 5.3.4 Shear stress/viscosity range
             5.4 Viscometer installation
             5.5 Type of control required
             5.6 Viscometer suitability
                 5.6.1 Size
                 5.6.2 Materials compatibility
                 5.6.3 Viscometer operating range changeover
                 5.6.4 Electrical and pneumatic supply requirements
                 5.6.5 Type of output required
                 5.6.6 Safety classification
             5.7 Viscometer operational considerations
                 5.7.1 Calibration
                 5.7.2 Accuracy and reproducibility
                 5.7.3 Cleaning and maintenance
                 5.7.4 Long term performance
                 5.7.5 Temperature control
             5.8 Capital and operating costs
         6. USE OF ON-LINE VISCOMETERS IN PROCESS CONTROL
             6.1 Long-term performance
             6.2 Ensuring that the measurement is meaningful
             6.3 What rheological property to measure
             6.4 Towards process control
             6.5 Summary of problems in application
         7. OPERATIONAL EXPERIENCE WITH ON-LINE VISCOMETERS AND RHEOMETERS FOR SLURRIES AND PASTES
             7.1 Preconditioning of sewage sludge to facilitate dewatering by filtration
         8. REFERENCES
         9 APPENDIX Suppliers of commercial on-line viscometers and rheometers
     Part 3: Slurry Flowmeters
         1. INTRODUCTION
             1.1 Objectives
             1.2 Scope of the Report
                 1.2.1 Secondary Instrumentation and Equipment
                 1.2.2 Cross-Correlation Flowmeters
             1.3 Further Information and Advice
             1.4 Advantages of Using this Report
         2. PROCEDURE FOR FLOWMETER SELECTION
             2.1 General Procedure
             2.2 Selection Steps 1-13 - Selection Criteria
             2.3 Selection Step 14 - Finalising Specifications
             2.4 Step 15 - Discussion with Manufacturers
             2.5 Advice on Procedure
                 2.5.1 Setting Requirements/Specifications
                 2.5.2 Order of Procedure
                 2.5.3 Rating System
                 2.5.4 Approach for the User who is Unfamiliar with Flowmeters
                 2.5.5 Approach for the Experienced Engineer
         3. SELECTION GUIDE
             3.1 Step 1 - Initial Specifications
                 3.1.1 Definition and Determination of Initial Specifications
                 3.1.2 Procedure
             3.2 Step 2 - Specific Limitations
                 3.2.1 Additional Comments Specific to Individual Meter Types
             3.3 Step 3 - Solids Concentration
                 3.3.1 General Considerations
                 3.3.2 Procedure
                 3.3.3 Additional Comments Specific to Individual Meter Types
             3.4 Step 4 - Particle Size
                 3.4.1 General Considerations
                 3.4.2 Procedure
                 3.4.3 Additional Comment Specific to Individual Meter Types
             3.5 Step 5 - Settling Slurries
                 3.5.1 Definition of a Settling Slurry
                 3.5.2 General Considerations
                 3.5.3 Procedure
                 3.5.4 Additional Comments Specific to Individual Meter Types
             3.6 Step 6 - Abrasion and Corrosion
                 3.6.1 General Comments
                 3.6.2 Procedure
                 3.6.3 Additional Comments Specific to Individual Meter Types
             3.7 Step 7 - Fouling
                 3.7.1 Procedure
                 3.7.2 Additional Comments Specific to Individual Meter Type
             3.8 Step 8 - Pulsating Flow
                 3.8.1 General Considerations
                 3.8.2 Procedure
                 3.8.3 Additional Comments Specific to Individual Meter Types
             3.9 Step 9 - Entrained Gas
                 3.9.1 General Considerations
                 3.9.2 Procedure
                 3.9.3 Additional Comments Specific to Individual Meter Types
             3.10 Step 10 - Non-Newtonian Flow Properties
                 3.10.1 General Considerations
                 3.10.2 Procedure
                 3.10.3 Additional Comments Specific to Individual Meter Types
             3.11 Step 11 - Installation Constraints
                 3.11.1 General Considerations
                 3.11.2 Procedure
                 3.11.3 Additional Comments Specific to Individual Meter Types
             3.12 Step 12 - Environmental Constraints
                 3.12.1 General Considerations
                 3.12.2 Procedure
                 3.12.3 Additional Comments Specific to Individual Meter Types
             3.13 Step 13 - Economic Constraints
                 3.13.1 General Considerations
                 3.13.2 Procedure
                 3.13.3 Additional Comments Specific to Individual Meter Types
             3.14 Step 14 - Finalising Specifications
         4. DISCUSSIONS WITH MANUFACTURERS (STEP 15)
             4.1 Check List for Electromagnetic Flowmeter
             4.2 Check List for Doppler Ultrasonic Flowmeter
             4.3 Check List for Transit-Time Ultrasonic Flowmeter
             4.4 Check List for Coriolis Effect Mass Flowmeter
             4.5 Check List for Venturi Flowmeter
             4.6 Check List for Orifice Plate Flowmeter
             4.7 Check List for Nozzle Flowmeter
             4.8 Check List for Wedge Flowmeter
             4.9 Check List for Target Meter
             4.10 Check List for Variable Area (Metal Tube Type) Meter
             4.11 Check List for Elbow Flowmeter
             4.12 Check List for Vortex-Shedding Flowmeter
             4.13 Check List for Thermal Mass Meter
             4.14 Check List for Slurry Turbine
             4.15 Check List for Level Measurement as a Means of Measuring Flow
             4.16 Check List for Flow Measurement Using a Suitable Positive Displacement Pump
         5. OPERATION OF FLOWMETERS
             5.1 Additional Considerations Specific to Each Meter Type
         6. COMPACT SELECTION GUIDE
             6.1 Compact Selection Procedure
         7. REFERENCES
         8. NOTATION
         9 APPENDIX A : BASIC OPERATING PRINCIPLES OF FLOWMETERS
             9.1 A1. Electromagnetic Flowmeter
                 9.1.1 A1.1 Velocity Profile Effects
                 9.1.2 A1.2 Optimisation of Flowmeter Design
                 9.1.3 A1.3 Coil Excitation
                 9.1.4 A1.4 Signal Noise
                 9.1.5 A1.5 Recent Developments
             9.2 A2. Doppler Ultrasonic Meter
                 9.2.1 A2.1 Electronics for Industrial Doppler Systems
                 9.2.2 A2.2 Pulsed Doppler Systems
             9.3 A3. Transit Time Ultrasonic Flowmeter
                 9.3.1 A3.1 General Principle of Operation
                 9.3.2 A3.2 Direct Transit Time Measurements
                 9.3.3 A3.3 Phase Measurement Techniques
                 9.3.4 A3.4 Sing-Around Technique
                 9.3.5 A3.5 Limitations of Clamp-on Transducers
                 9.3.6 A3.6 Frequency of Operation
             9.4 A4. Coriolis-Type Mass Meter
                 9.4.1 A4.1 General Operating Principle
                 9.4.2 A4.2 Additional Measurements
                 9.4.3 A4.3 Performance Aspects
                 9.4.4 A4.4 Standardisation
                 9.4.5 A4.5 Future Developments
             9.5 A5. Principle of Differential Pressure Flowmeters - Venturi, Orifice Plate, Nozzle and Wedge Meter
                 9.5.1 A5.1 General Operating Principles
                 9.5.2 A5.2 Venturi Meter
                 9.5.3 A5.3 Orifice Plate
                 9.5.4 A5.4 Nozzle
                 9.5.5 A5.5 Wedge Meter
             9.6 A6. Other Flowmeters Utilising Pressure Difference - Target (Drag Plate Meter) and Variable Area Meters
                 9.6.1 A6.1 Target Meter (Drag PLate)
                 9.6.2 A6.2 Variable Area Meters
                 9.6.3 A6.3 Elbow Flowmeter
             9.7 A7. Vortex Shedding Meter
                 9.7.1 A7.1 Frequency Sensing Systems
             9.8 A8. Thermal Mass Flowmeters
             9.9 A9. Slurry Turbine Flowmeter
             9.10 A10. Measurement of the Rise or Fall of a Level in a Tank
                 9.10.1 A10.1 Continuous Level Measurement Sensors
             9.11 A11. The Use of a Suitable Pump for Measuring the Flow
             9.12 A12. Cross-Correlation Flowmeter
         10 APPENDIX B : MANUFACTURERS
             10.1 FLOWMETER MANUFACTURERS
                 10.1.1 Electromagnetic Flowmeters
                 10.1.2 Doppler Ultrasonic and Transit-time Ultrasonic Meters
                 10.1.3 Coriolis Mass Flowmeters
                 10.1.4 Venturi, Orifice, Nozzle and Target Meters
                 10.1.5 Wedge Meter
                 10.1.6 Variable-Area Meters
                 10.1.7 Vortex-Shedding Meters
                 10.1.8 Thermal Mass Meter
                 10.1.9 Turbine Meters
             10.2 MANUFACTURERS OF LEVEL MEASUREMENT SENSORS
             10.3 MANUFACTURERS OF POSITIVE DISPLACEMENT PUMPS
             10.4 NAMES AND ADDRESSES OF MANUFACTURERS
     Part 4: Moisture Measurement
         1. INTRODUCTION
             1.1 Objective and Scope of Report
             1.2 Explanation of Terms and Moisture States in a Particulate Solid
             1.3 An Overview of On-Line Moisture Measurement
                 1.3.1 Introduction
                 1.3.2 Overview of Methods for Wet Bulk Solids
                 1.3.3 Overview of Methods for Slurries and Pumpable Pastes
                 1.3.4 Liquids Other than Water
         2. GUIDE TO SELECTION OF A SUITABLE SENSOR
             2.1 Introduction
             2.2 Problem Definition
             2.3 Non-pumpable Wet Bulk Solids
                 2.3.1 Economic Constraints
             2.4 Pumpable slurry or paste in a pipe
             2.5 Slurry or paste in agitated storage vessel
             2.6 Example of sensor selection
                 2.6.1 The Problem
                 2.6.2 Alternatives
                 2.6.3 Conclusion
         3. MOISTURE MEASUREMENT TECHNIQUES
             3.1 Direct Moisture Measurement of Bulk Solids
                 3.1.1 Infrared Diffuse Reflectance
                 3.1.2 Neutron Moderation
                 3.1.3 Low Resolution Nuclear Magnetic Resonance (NMR)
             3.2 Inferential Determination of Moisture Content in Bulk Solids
                 3.2.1 Microwave Absorption
                 3.2.2 Capacitance
                 3.2.3 Equilibrium Relative Humidity
             3.3 Inferential Techniques using Density measurement of Slurries in Pipeflow
                 3.3.1 Gravimetric methods
                 3.3.2 Radiometric absorption
                 3.3.3 Vibration Type
                 3.3.4 Coriolis force mass flow/density meters
                 3.3.5 Counter-Flowmeter or "U-loop" for Settling Slurries
             3.4 Inferential Techniques using other Physical Property Measurement for Slurries in Pipeflow
                 3.4.1 Electrical conductivity and capacitance
                 3.4.2 Optical methods
                 3.4.3 Ultrasonic techniques
                 3.4.4 Viscometric methods
                 3.4.5 Volumetric flowmeters
             3.5 On-line Density Measurement Techniques for Storage Tanks
                 3.5.1 Static pressure methods
                 3.5.2 Buoyancy methods
                 3.5.3 Radiometric reflection
         4. FACTORS AFFECTING SENSOR SELECTION
             4.1 Operational Factors
                 4.1.1 Why Measure Moisture On-Line?
                 4.1.2 Open / Closed System
                 4.1.3 Flowing / stationary
                 4.1.4 Sampling / bulk measurement
                 4.1.5 Product contact
             4.2 Instrument Factors
                 4.2.1 Cost
                 4.2.2 Response time
                 4.2.3 Accuracy and reliability
                 4.2.4 Ease and frequency of calibration
                 4.2.5 Penetration depth required
                 4.2.6 Robustness
         5. PROBLEMS WITH MOISTURE DETERMINATION
             5.1 Sampling
             5.2 Air or other gas incorporation
                 5.2.1 Methods to remove gas before measurement
             5.3 Phase separation
                 5.3.1 At equipment boundaries
                 5.3.2 Resulting from gravity or other body forces
             5.4 Non-uniform moisture distribution (other than phase separation)
             5.5 Abrasion, deposition and fouling
         6. NOMENCLATURE
         7. REFERENCES
         8. APPENDIX A : MANUFACTURERS OF SENSORS FOR MOISTURE MEASUREMENT IN WET BULK SOLIDS
         9. APPENDIX B : INTERRELATION BETWEEN SLURRY DENSITY ( r m) AND CONCENTRATION BY VOLUME (Cv) AND MASS (Cm)
         10 APPENDIX C : MANUFACTURERS OF ON-LINE DENSITY METERS FOR SLURRIES AND PASTES
     Part 5: Selection, Installation and Operation of On-line Viscometers
         1. INTRODUCTION
             1.1 Report objectives
             1.2 Report scope
             1.3 Advice on the use of the report
         2. REASONS FOR USING ON-LINE VISCOMETRY
         3. SUMMARY CLASSIFICATION OF VISCOMETER TYPES
             3.1 Rotational viscometers
                 3.1.1 Coaxial cylinder viscometers
                 3.1.2 Rotating bob viscometer
                 3.1.3 Nutating cylinder viscometer
                 3.1.4 Parallel plate viscometer
                 3.1.5 Rotating disc viscometer
             3.2 Tube or pipe viscometers
                 3.2.1 Full bore pipe viscometer
                 3.2.2 Capillary tube viscometer
             3.3 Moving cylinder viscometers
             3.4 Drag on blade viscometers
             3.5 Moving blade viscometers
             3.6 Squeeze flow viscometers
             3.7 Vibrational viscometers
         4. SPECIFICATION OF REQUIREMENTS FOR VISCOMETER
             4.1 Material considerations
                 4.1.1 Type
                 4.1.2 Physical properties relevant to viscosity measurement
             4.2 Process operating conditions
                 4.2.1 Temperature
                 4.2.2 Pressure
                 4.2.3 Flow regime at measuring point
             4.3 Viscometer operating range
                 4.3.1 Viscosity or consistency measurement
                 4.3.2 Temperature
                 4.3.3 Pressure
                 4.3.4 Shear rate range
                 4.3.5 Shear stress / viscosity range
             4.4 Viscometer installation
             4.5 Type of control required
             4.6 Viscometer suitability
                 4.6.1 Size
                 4.6.2 Materials compatibility
                 4.6.3 Viscometer operating range changeover
                 4.6.4 Electrical and pneumatic supply requirements
                 4.6.5 Type of output required
                 4.6.6 Safety classification
             4.7 Viscometer operational considerations
                 4.7.1 Calibration
                 4.7.2 Accuracy and reproducibility
                 4.7.3 Cleaning and maintenance
                 4.7.4 Long term performance
                 4.7.5 Temperature control
             4.8 Capital and operating costs
         5. PROCEDURE FOR VISCOMETER SELECTION
             5.1 How to use this section
         6. DISCUSSION WITH SUPPLIERS
         7. VISCOMETER INSTALLATION AND OPERATION
             7.1 Rotational viscometers
                 7.1.1 Coaxial cylinder viscometer
                 7.1.2 Rotating bob viscometer
                 7.1.3 Nutating cylinder viscometer
                 7.1.4 Parallel plate viscometer
                 7.1.5 Rotating disc viscometer
             7.2 Drag on blade viscometer
             7.3 Squeeze flow viscometer
             7.4 Vibrational viscometers
         8. TRIALS TO CONFIRM SELECTION
             8.1 Situations where this is desirable
             8.2 Setting up trials
                 8.2.1 Manufacturer's test facilities
                 8.2.2 Viscometer loan or hire
                 8.2.3 Test at independent laboratory
         9. A WORKED EXAMPLE USING THIS DESIGN GUIDE
             9.1 Soup/Water Interfacial Detection
                 9.1.1 Description of the problem
                 9.1.2 Setting up the viscometer design specification
                 9.1.3 Viscometer selection and identification
         10. REFERENCES
         APPENDIX A VISCOMETER SPECIFICATION DATA SHEET
         APPENDIX B SUPPLIERS OF COMMERCIAL ON-LINE VISCOMETERS AND RHEOMETERS
     Part 6: Survey of On-line Level Measurement Techniques
         SUMMARY
         1. INTRODUCTION
         2. CONSIDERATIONS FOR INSTRUMENT SELECTION
         3. DESCRIPTION OF BASIC SENSOR SYSTEMS
             3.1 Float Level Sensors
                 3.1.1 Float Switches
                 3.1.2 Continuous-indicating Float Systems
             3.2 Displacer Type Level Sensors
                 3.2.1 Displacer level switches
                 3.2.2 Continuous displacer level systems
             3.3 Servo (Tape) Type Level Systems
                 3.3.1 Float-actuated servo level gauges
                 3.3.2 Displacer-activated servo level gauges
                 3.3.3 Plumb line level gauges
                 3.3.4 Comments on liquid service servo gauges
             3.4 Capacitance Level Sensors
                 3.4.1 Capacitance level switches
                 3.4.2 Continuous capacitance level systems
             3.5 Radio Frequency/Admittance Level Systems
             3.6 Conductivity Level Switches
             3.7 Nuclear Radiation Level Sensors
             3.8 Microwave Barrier Level Switch
             3.9 Rotating Paddle Level Switches
             3.10 Tilt Level Switches
             3.11 Thermal Level Switches
             3.12 Optical Level Switches
             3.13 Vibrating Rod or Tuning Fork Level Switches
             3.14 Ultrasonic Level Sensors
                 3.14.1 Damped ultrasonic level switches
                 3.14.2 Transmission ultrasonic switches
                 3.14.3 Pulse Echo Continuous Ultrasonic Level Sensors
             3.15 RADAR Level Sensors
             3.16 LASER Level Systems
             3.17 Guided Wave Reflectometry Systems
             3.18 Hydrostatic Head Level Systems
                 3.18.1 Pressure transducer level systems
                 3.18.2 Differential pressure transducer systems
                 3.18.3 Gas bubbler systems
                 3.18.4 Resistance tape level sensor
                 3.18.5 Diaphragm level switches
             3.19 Weight and Chain Level Systems
             3.20 Other Restricted Application Systems
         4. METHODS UNDER DEVELOPMENT
         5. PROBLEM AREAS IN LEVEL MEASUREMENT
             5.1 Temperature of Vessel Environment
             5.2 Pressure of Vessel Environment
             5.3 Compatibility of Materials of Construction
             5.4 Boiling, Bubbling, or Aerated Materials
             5.5 Foaming Liquids
             5.6 Stirred or Agitated Vessels
             5.7 Hard-to-Handle Materials
             5.8 Liquid-Liquid and Liquid-Solid Interface Detection
             5.9 Variable Specific Gravity or Bulk Density
             5.10 Vapour or Dusty Environments Above the Material Surface
             5.11 Angle of Repose of Solids
             5.12 Application in Hazardous Areas
         6. CONCLUDING REMARKS
         APPENDIX A: LEVEL EQUIPMENT MANUFACTURERS BASED IN EUROPE
         APPENDIX B: LEVEL EQUIPMENT MANUFACTURERS BASED IN NORTH AMERICA
         APPENDIX C: LEVEL MEASURING TECHNIQUES AVAILABLE FROM GIVEN SOURCES
             Appendix C.1 European and UK Suppliers
                 Appendix C.1.1 European and UK Suppliers
             Appendix C.2 North American Manufacturers
                 Appendix C.2.1 North American Manufacturers
     Part 7: Selection Guide for Level Measurement of Slurries
     Part 8: The Application of Passive Acoustic Emission Monitoring to Slurry Handling Systems
         SUMMARY
         1 INTRODUCTION
             1.1 Acoustic Emission Background
             1.2 Definition of Acoustic Emission
             1.3 Stresswave Propagation Modes
             1.4 Principle of Operation of Passive AE Sensors
                 1.4.1 Piezo-electric (PZT) AE Sensors
                 1.4.2 Optical AE Sensors
                 1.4.3 Capacitive (PETP) Film AE Sensor
             1.5 Sources of AE Activity
         2. MODERN INSTRUMENTATION
             2.1 AE Sensors
                 2.1.1 Narrowband AE Sensors
                 2.1.2 Wideband AE Sensors
                 2.1.3 Selection of Optimum AE Sensor Frequency
             2.2 AE Sensor Products
                 2.2.1 Portable Systems
                 2.2.2 Permanent Systems
             2.3 AE Instrumentation Manufacturers' Database
                 2.3.1 PZT Crystals
                 2.3.2 Conventional AE Sensors and Systems
                 2.3.3 AE-based Products
                 2.3.4 Hand Held/Portable Products
         3. SIGNAL CONDITIONING TECHNIQUES
             3.1 Event Counting
             3.2 Simple Amplitude Output
             3.3 Higher Level Amplitude Parameters
                 3.3.1 Holroyd's 'Distress'
                 3.3.2 Rate of Change Alarm
             3.4 De-Modulated Narrowband Frequency Data
             3.5 Wideband data
         4. MULTI-VARIATE POST-PROCESSING TECHNIQUES
             4.1 Multivariate Calibration Techniques
         5. AV TECHNOLOGY'S ACOUSTIC PROCESS MONITORING METHOD
             5.1 AE Instrumentation
                 5.1.1 Signal Conditioning
                 5.1.2 Data Pre-Processing
                 5.1.3 Modelling
             5.2 Acoustic Process Monitoring Feasibility Study
                 5.2.1 Stage 1: Assess Suitability
                 5.2.2 Stage 2: Calibration
                 5.2.3 Stage 3: Process Predictions
         6. ILLUSTRATION 1 - SLURRY MONITORING TRIALS AT AEA HARWELL
             6.1 Introduction
             6.2 Experimental Arrangement
             6.3 Test Programme
             6.4 Data Acquisition
             6.5 Data Processing
             6.6 Multivariate Calibration
             6.7 Results
             6.8 Conclusions
         7. ILLUSTRATION 2 - HYDROCYCLONE SEPARATION PROCESS
             7.1 Introduction
             7.2 Experimental Arrangement
                 7.2.1 Hydrocyclone Apparatus and Feed Materials
                 7.2.2 Acoustic Emission Measurements
             7.3 Signal Processing and Calibration
                 7.3.1 Data Processing
                 7.3.2 Calibration
             7.4 Spectral Results
                 7.4.1 Solids Concentration and Flowrate
                 7.4.2 Spray-Rope-Blockage Transitions and Underflow Blockage
                 7.4.3 Effect of Particle Size
             7.5 Process Predictions
                 7.5.1 Pressure Drop and Solids Concentration Predictions
                 7.5.2 Stream Volume, Mass and Density Predictions
                 7.5.3 Stream Particle Size Predictions
                 7.5.4 Underflow Fault Condition Predictions
             7.6 Conclusions
         8. CONCLUDING REMARKS
             8.1 Benefits of Acoustic Process Monitoring
         9 REFERENCES
         10. APPENDIX A : EXAMPLES OF AE DATA
             10.1 Wrist Watch Example
             10.2 Hyper Compressor Example
             10.3 Valve Leakage Example
             10.4 Slurry Pipe Flushing Example
             10.5 Cement Mixing Example
             10.6 PCA Score Plot Example
             10.7 Pipework Leak Detection Example

Volume SH 7: Part 1 On-line Level Measurement Techniques

This part outlines the techniques available for level measurement in the process industries and relates to all aspects of material state. The appendices give a ready guide to potential users as to the sources of manufacturers and more relevant applications in wet solids handling. The survey has been restricted to those sources which can give a remote signal output, whether electrical or pneumatic, rather than local visual indication only. The part is being updated to include suppliers’ details and products offered in North America and Europe.


Volume SH 7: Part 2 On-line Viscosity and other Rheological Techniques

This part describes the various types of commercially-available (and obsolete) on-line instruments to measure viscosity or consistency. The term consistency is used when an instrument is unable to measure absolute viscosity. A brief description of each viscometer type together with its advantages, limitations and application areas is given. Although more generally used with polymers, on-line rheometers, as distinct from viscometers, which measure rheological properties other than viscosity (e.g., complex dynamic viscosity and normal stress) are also described. This was done as the rheological property in question may be more sensitive to changes in, for instance, slurry composition. An overview of the different on-line instruments which have been built in-house is also given.

Factors influencing viscometer selection such as operating temperature, operating pressure, flow condition at the required measuring point, and shear rate range to be covered by the instrument are discussed.

Despite the wide instrument availability, industrial application of on-line viscosity and rheological measurement for process control is not as widespread as expected. This report outlines the fundamental reasons for this and discusses how this problem might be addressed. Some case studies on the successful application of on-line viscometers/rheometers in slurry/paste service are described.


Volume SH 7: Part 3 Slurry Flowmeters

 The objective of this part is to guide a potential user in the selection installation and operation of flowmeters for dirty liquid and slurry applications and to provide sufficient information for the user to carry out fruitful discussions with manufacturers. The selection procedure is illustrated by a flow chart and is both simple and flexible. The report has been designed in such a way that it provides a comprehensive guide for the user who is unfamiliar with flowmeters as well as a fast selection procedure, condensed to a few pages, for the experienced engineer.


Volume SH 7: Part 4 On-line Densitometers

This part covers gravimetric methods, radiometric absorption, vibrating tube techniques, Coriolis force mass flowmeters, and, in the case of coarse particle settling slurries, the counter flowmeter or "U-loop". In addition, to direct measurement of slurry density on-line, there are several inferential techniques for moisture content in slurries, including the use of electrical conductivity and capacitance, optical methods, ultrasonic techniques, viscometric methods, and the adaptation of specific designs of volumetric flowmeters.


Volume SH 7: Part 5 Selection of On-line Viscometers

This part provides a coherent logical methodology to selecting an on-line viscometer for a slurry/paste application. Guidance on the installation and operation of on-line viscometers is also given. The report is based on Part 2 and information derived from viscometer users and suppliers. The first four sections provide a brief guide to the various types of on-line viscometers that are commercially available and deals with the key parameters governing the viscometer selection process. Section 5 provide the methodology, including flow charts, for obtaining a shortlist of suitable on-line viscometers for the application under consideration. Section 6 gives some guidance on the discussions that should take place with the potential supplier(s) of the shortlisted viscometers. Section 7 outlines the various considerations for viscometer installation and operation. Section 8 describes the trials that should be taken to confirm the viscometer selection. Section 9 gives a worked example on the use of this guide. Appendix A gives the viscometer specification data sheet to be used in conjunction with Section 5. Appendix B is a comprehensive listing of suppliers of commercial on-line viscometers/rheometers together with address, telephone and facsimile details.


Volume SH 7: Part 6 Selection Guide for Level Measurement

This part will provide a selection guide based on the updated survey of level measurement methods outlined in Part 1


Volume SH 7: Part 7 Passive Acoustic Emission Monitoring applied to Slurry Systems

This part reviews the potential of the technique of monitoring industrial processes using acoustics. This is a proven and extremely powerful measurement technique. In particular systems based upon the interpretation of much higher frequency structure borne acoustic emissions (AE) at typically 50 kHz to 1 MHz can offer numerous advantages over conventional techniques, often offering totally unique monitoring opportunities.

The monitoring of process conditions using AE is not new. The use of acoustic emissions to monitor chemical reactions dates back 15 years, whilst the interpretation of AE measurements using advanced pattern recognition methods has been successfully used for over 8 years. However, with the advancement of the power of the common PC, the use of AE data for industrial monitoring applications is becoming increasingly viable, with an increasing number of commercial systems now on the market and many more research and development applications currently being considered.

It is widely accepted that for many monitoring applications, the AE technique can offer many advantages over conventional instrumentation. For many users, the most advantageous feature of passive AE monitoring is the truly non-invasive clamp-on nature of the instrumentation, enabling externally applied sensors to ‘listen’ to process conditions occurring within non-accessible plant and machinery.

Another main advantage is the potential of the calibrated AE system to replace difficult periodic manual sampling operations with continuous process monitoring capabilities, thereby offering obvious benefits in terms of system optimisation.

Other advantages are afforded in supervisory monitoring applications, where the simplest AE system can be used to detect a change from a desired steady state condition, thereby drawing attention to a potential problem and alerting an operator to provide the necessary intelligence to be able to diagnose any process problems. For example, a continuous steady state process may be adversely affected by unwanted variations in any of a number of parameters, including:

  • Material composition
  • Flowrates
  • Particle size distributions
  • Density changes
  • Temperature
  • Pressure etc.

On the other hand, a non-intelligent AE system could simply detect that something significant had changed because the process now sounded ‘different’.

This state of the art review details the current practice of Acoustic Emission (AE) monitoring and provides a brief outline of the wide range of possible applications in order to highlight the tremendous capabilities of the technique, particularly for slurry monitoring applications.

In the near future, it is expected that the use of passive acoustic emission will become much more widespread as the results of the numerous current ongoing evaluations produce real process monitoring successes and in so doing, draw further attention to the method whilst also revealing the most suitable applications for this technique. At this stage it is likely that the form of the AE monitoring instrumentation will also change, to become less like general purpose evaluation equipment and to evolve into more dedicated products targeting specific process applications.