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DRY 11: Dryer Operations

DRY 11: Dryer Operations
     Part 2: Control and Instrumentation
         1 INTRODUCTION AND OVERVIEW
             1.1 Aims and Scope
             1.2 Summary of Contents
             1.3 An Overview of Process Control and Instrumentation
             1.4 Current Industrial Practice in Control of Dryers
         2 OPERATING AND CONTROL STRATEGY
             2.1 The Objectives of Process Control
                 2.1.1 Inventory Management and Production Control
                 2.1.2 Extent of Manual Intervention
                 2.1.3 Plant Utilisation Targets and Maintenance Strategy
                 2.1.4 Product Quality Control and Assurance
                 2.1.5 Material and Energy Costs
                 2.1.6 Management Information
                 2.1.7 Process Diagnostics
                 2.1.8 Process Safety, Health and Environmental Performance
             2.2 Process Control Strategies
                 2.2.1 Alarms and Interlocks
                 2.2.2 Process Control
                 2.2.3 Quality Control
                 2.2.4 Mode of Operation (Management information etc)
                 2.2.5 Inventory Control
         3 THE MAIN CONTROL VARIABLES
             3.1 Introduction
             3.2 Feed Flow Rate
                 3.2.1 Liquid Feeds
                 3.2.2 Solid Feed
                 3.2.3 Batch Dryers
             3.3 Feed Moisture Content
             3.4 Product Flow Rate
             3.5 Product Moisture
             3.6 Gas Flow
             3.7 Gas Temperature
                 3.7.1 Inlet Temperature
                 3.7.2 Outlet Temperature
             3.8 Gas Humidity
                 3.8.1 Inlet Humidity
                 3.8.2 Outlet Humidity
             3.9 Gas Composition
             3.10 Gas Pressure
                 3.10.1 Vacuum Dryers
                 3.10.2 Atmospheric Dryers
             3.11 Particulates in the Gas Stream
                 3.11.1 Gas Inlet
                 3.11.2 Gas Outlet
             3.12 Energy Input
                 3.12.1 Steam/Hot Water
                 3.12.2 Natural Gas
                 3.12.3 Electricity
         4 BASIC CONTROL PRINCIPLES
             4.1 Elements of an Automatic Process Control System
                 4.1.1 Sensors and Measurement
                 4.1.2 The Controller
                 4.1.3 Signal Transmission
                 4.1.4 Implementing the Control Action
             4.2 Types of Automatic Process Control Systems
                 4.2.1 Open loop control
                 4.2.2 Closed loop control
                 4.2.3 Advanced Control
             4.3 Principles of Control System Design
         5 MEASUREMENT
             5.1 Introduction
             5.2 Temperature
                 5.2.1 Thermocouples
                 5.2.2 Resistance thermometers
                 5.2.3 Expansion thermometers
                 5.2.4 Radiation thermometers
             5.3 Pressure
                 5.3.1 Manometers
                 5.3.2 Bourdon Gauge
                 5.3.3 Diaphragm
                 5.3.4 Bellows
                 5.3.5 Location and Installation of Pressure Tappings
             5.4 Gas Flow
                 5.4.1 Pitot Tube
                 5.4.2 Differential Pressure Meter
                 5.4.3 Vortex Meter
                 5.4.4 Location of Flow Measurement
                 5.4.5 Exploratory Measurement
             5.5 Solids Flow
                 5.5.1 Weight
                 5.5.2 Volume
                 5.5.3 Momentum
             5.6 Humidity
                 5.6.1 Mechanical Hygrometer
                 5.6.2 Psychrometer (Wet & Dry Bulb Thermometer)
                 5.6.3 Electrical Measurement
                 5.6.4 Dew Point Measurement
                 5.6.5 Infra-Red Gas Analysers (IRGA)
                 5.6.6 Precision and Accuracy
             5.7 Moisture in Solids
                 5.7.1 Capacitance
                 5.7.2 Infrared
                 5.7.3 Chilled Mirror Dew Point Meter.
                 5.7.4 Electrical Conductivity
                 5.7.5 Laboratory Techniques
                 5.7.6 Slurry Density
             5.8 Particle Size/Distribution
             5.9 Particle Concentration
                 5.9.1 Impingement
                 5.9.2 Optical
             5.10 Other Product Properties
         6 TYPES OF CONTROLLER
             6.1 Introduction
             6.2 Single Loop Controller
             6.3 Smart Controllers
                 6.3.1 Additional Alarm Levels
                 6.3.2 Self Tuning
                 6.3.3 Self Diagnostics
             6.4 Multi-Loop Controllers
             6.5 `Computer' Control
             6.6 Distributed Control System
             6.7 Future Trends
         7 CONTROL OF INDUSTRIAL DRYER TYPES
             7.1 Introduction
             7.2 The Control of Batch Dryers
                 7.2.1 Batch Atmospheric Tray Dryers
                 7.2.2 Batch Vacuum Tray Dryers
                 7.2.3 Through-Circulation Batch Dryers
                 7.2.4 Batch Agitated Dryers
                 7.2.5 Batch Fluid Beds
                 7.2.6 Special Batch Dryers
             7.3 Control of Continuous Dryers
                 7.3.1 Continuous Cross-Circulation Tray and Band Dryers
                 7.3.2 Continuous Through-Circulation Dryers
                 7.3.3 Continuous Horizontal Agitated Dryers
                 7.3.4 Rotary Layer Dryers
                 7.3.5 Rotary Dispersion Dryers
                 7.3.6 Continuous Fluid Beds
                 7.3.7 Pneumatic Conveying Dryers
                 7.3.8 Spray Dryers
                 7.3.9 Drum Dryers
                 7.3.10 Combination Dryers
                 7.3.11 Cylinder Dryers
                 7.3.12 Multi-Stage Dryers
         8 SIGNAL TRANSMISSION, ACTUATORS AND CONTROL VALVES
             8.1 Introduction
             8.2 Signal Transmission
                 8.2.1 Pneumatic Signals
                 8.2.2 Analogue Electrical Signals
                 8.2.3 Digital Electrical Signals
             8.3 Actuation
             8.4 Control Valves
         9 PROJECT FACTORS AFFECTING CONTROL SYSTEM DESIGN
             9.1 Introduction
             9.2 Design
             9.3 Siting and Installation
             9.4 Maintenance
             9.5 Hazards Associated with Instrumentation
             9.6 Vendor Selection
         10 CONCLUSIONS AND FUTURE TRENDS
         11 REFERENCES
         12 NOMENCLATURE
         13 APPENDIX 1 SOME BASIC PRINCIPLES OF CONTROL SYSTEMS
             13.1 Time Dependent Elements
                 13.1.1 Dead time
                 13.1.2 Resistance-capacitance lag
             13.2 The Measuring Element
             13.3 The Control Element
             13.4 The Transfer Function
             13.5 System Gains
             13.6 Types of Control Action
                 13.6.1 Discontinuous control
                 13.6.2 Continuous control
             13.7 Problems of Stability
             13.8 Problems of Dynamics
         14 APPENDIX 2 AUTOMATIC PROCESS CONTROLLERS
             14.1 Classification of Controllers
                 14.1.1 Self-operating controller
                 14.1.2 Externally-operated controllers
                 14.1.3 The Final Control Element
             14.2 Tuning of Controllers
     Part 3: Dryer Troubleshooting
         1. INTRODUCTION
             1.1 Scope of this Section of the Manual
             1.2 An Overview of Dryer Troubleshooting
         2. METHODOLOGY
             2.1 Problem Definition
             2.2 Data Gathering
                 2.2.1 Process Instrument Data
                 2.2.2 Design Data
                 2.2.3 Exploratory Measurements
                 2.2.4 Product Quality Measurements
                 2.2.5 Operator Observations
             2.3 Data Analysis
                 2.3.1 Heat and Mass Balance Discrepancies
             2.4 Performance Comparisons
             2.5 Conclusions and Actions
             2.6 Performance Auditing
         3. PROBLEM CATEGORIES
             3.1 Commissioning
             3.2 Start-Up and Shut-Down
             3.3 Safety, Health and Environmental Problems
             3.4 Drying Performance Problems
             3.5 Product Quality Problems (non-moisture)
                 3.5.1 Bulk Density
                 3.5.2 Colour (particularly whiteness or clarity)
                 3.5.3 Contamination
                 3.5.4 Taste / Smell
             3.6 Material Handling Problems
                 3.6.1 Blockages at feed or discharge point
                 3.6.2 Internal Build-Up
                 3.6.3 Elutriation of Fines
                 3.6.4 Dry Product Flowability
             3.7 Control and Variability
             3.8 Equipment Failure
             3.9 People Problems
         4. TROUBLESHOOTING ON PARTICULAR TYPES OF DRYER
             4.1 Continuous Dryers
                 4.1.1 Pneumatic Conveying Dryers
                 4.1.2 Fluidised Bed Dryers
                 4.1.3 Rotary Dryers
                 4.1.4 Spray Dryers
                 4.1.5 Through Circulation Band Dryers
             4.2 Batch Dryers
                 4.2.1 Tray Dryers
                 4.2.2 Fluid Bed Dryers
                 4.2.3 Batch Agitated Dryers
         5. AN ALGORITHM FOR DRYER TROUBLESHOOTING
             5.1 Introduction
             5.2 The Basic Algorithm
             5.3 Symptoms and Causes of Problems
                 5.3.1 Performance
                 5.3.2 Handling
                 5.3.3 Product Quality
                 5.3.4 Safety and Environmental
         6. EXAMPLES OF DRYER TROUBLESHOOTING
             6.1 Performance
                 6.1.1 Energy
                 6.1.2 Throughput
                 6.1.3 Moisture Content
             6.2 Material Handling
                 6.2.1 Feed Point Blockage of Pneumatic Conveying Dryer
                 6.2.2 Build-Up in a Ring Dryer
                 6.2.3 Build-Up in a Fluid Bed Dryer
                 6.2.4 Dryer Discharge Problem with Needle-Shaped Crystals
                 6.2.5 Free-flowing Product from the Dryer becomes Sticky in the Cooler
                 6.2.6 Electrostatic Charges on Dry Product
                 6.2.7 Water of Crystallisation
                 6.2.8 Agitation on a Filter Dryer
             6.3 Product Quality
                 6.3.1 Door Leaks on a Tray Dryer
                 6.3.2 Hard Particles from a Spray Dryer
                 6.3.3 Dusty Spray Dryer Product
             6.4 Safety and Environmental
                 6.4.1 Combustible Material -1
                 6.4.2 Combustible Material -2
                 6.4.3 Reducing Volume of Effluent Gases to be Treated
         7. REFERENCES
     Part 4: Ways of Reducing Energy Consumption in Dryers
         1. INTRODUCTION
         2. DESIGN GUIDE
             2.1 Introduction
             2.2 Existing Plant
                 2.2.1 Strategy
                 2.2.2 Example
             2.3 New Plant
         3. ANALYSING THE OPERATION OF AN EXISTING DRYER
             3.1 Introduction
             3.2 Heater Modules
                 3.2.1 Introduction
                 3.2.2 Indirect Heater Module
                 3.2.3 Direct-fired Heater Module
             3.3 Continuous Dryer Modules
                 3.3.1 Introduction
                 3.3.2 Continuous Convection Dryer Module
                 3.3.3 Continuous Contact Dryer Module
                 3.3.4 Continuous Vacuum Dryer Module
             3.4 Batch Dryer Modules
                 3.4.1 Introduction
                 3.4.2 Batch Convection Dryer Module
                 3.4.3 Batch Contact Dryer Module
                 3.4.4 Batch Vacuum Dryer Module
             3.5 Heat Recovery Modules
                 3.5.1 Introduction
                 3.5.2 Waste Heat Exchanger Module
                 3.5.3 Product Cooler Module
             3.6 Linking the Modules
             3.7 Measurement Techniques
             3.8 Routine Monitoring of Heat Consumption
         4. REDUCING ENERGY CONSUMPTION WITH NEGLIGIBLE OR MlNOR CAPITAL EXPENDITURE
             4.1 Improved Housekeeping
             4.2 Reduction of the Air Supply Rate
             4.3 Changes in Production Schedules
             4.4 Improved Instrumentation and Control
                 4.4.1 Principles
                 4.4.2 Present State of Development
         5. REDUCING ENERGY CONSUMPTI0N WITH SlGNIFICANT CAPITAL EXPENDITURE
             5.1 Introduction
             5.2 Improved Dewatering of the Dryer Feedstock;
             5.3 Heat Recovery from the Exhaust Gas
                 5.3.1 Introduction
                 5.3.2 Tubular Heat Exchangers
                 5.3.3 Plate Heat Exchangers
                 5.3.4 Heat Wheels
                 5.3.5 Heat Pipes
                 5.3.6 Run-around Coils
                 5.3.7 Fluidised Bed Heat Exchangers
                 5.3.8 Heat Pumps
                 5.3.9 Wet Scrubbers
             5.4 Heat Recovery from the Product
             5.5 Recycle of Exhaust Air
             5.6 Switching from an Indirect to a Direct-Fired Heater
             5.7 Utilisation of Process Waste Heat
             5.8 Advanced Data-Logging and Control Systems
             5.9 Conclusions
         6. MINIMISING ENERGY CONSUMPTI0N OF NEW PLANT
             6.1 Introduction
             6.2 Elimination of the Dewatering Step
             6.3 Preconcentration of Feedstocks by more Efficient Water Removal Techniques
                 6.3.1 Liquid Feedstocks
                 6.3.2 Slurry Feedstocks
             6.4 Dryer Selection for Minimum Energy Consumption
                 6.4.1 Two-stage Drying
                 6.4.2 Contact Dryers
             6.5 Carver Greenfield Process
             6.6 Substitution of Water by Organic Solvents
                 6.6.1 Displacement Drying
                 6.6.2 Drying of Solvent-based Feedstocks
             6.7 Conclusions
         7. NEW TECHNOLOGY FOR REDUCING ENERGY CONSUMPTION
             7.1 Introduction
             7.2 High-temperature Closed-cycle Heat pumps
             7.3 Open-cycle Heat Pumps
             7.4 Drying through Flash Evaporation under Vacuum
             7.5 "Free Heat" Sources
             7.6 Conclusions
         8. REFERENCES
         9. NOMENCLATURE
     Terms and Conditions of Use

See also: Mini-Manual MM I. The practical determination of gas and particle properties

Volume DRY XI Part 1 Introduction.


Volume DRY XI Part 2 Control and operation of dryers.

Effective control methods are vital for the efficient and safe operation of dryers, and they depend in turn on the information provided by plant instrumentation, both in its extent and accuracy. This Part reviews the current state of control and instrumentation of industrial dryers, in their context as a unit operation usually integrated into a multi-operation process plant.

After a brief introduction, Section 2 gives an overview of the operating and control strategy for an entire plant. Next, the variables which can be controlled are listed, and basic principles of control are reviewed. The available measurement methods are reviewed, with cross-references to Mini-Manual I (Determination of Gas and Particle Properties) which covers this subject in more detail. There are descriptions of the available types of controllers, actuators and signal transmission methods, and other aspects of the control system such as siting, maintenance and hazards are briefly summarised. There is also an extensive section detailing how control methods are applied to the major individual dryer types.


Volume DRY XI Part 3 Dryer troubleshooting.

Dryer troubleshooting and problem-solving is a vital area which has been almost totally neglected in published literature. It presents a complex problem because of the wide range of possible problems, causes and solutions. However, the broad classes of problem and the most common solutions can be given, and a methodology has been defined which allows the engineer to narrow down the possibilities. Specific examples are provided; these may be directly relevant to the user's problem, or may suggest ideas which lead to a solution by a parallel approach.

Part 3 begins with an introduction and an overview of dryer troubleshooting. The terminology and the stages of the troubleshooting process are defined, and dryer problems are categorised. The next section gives a methodology for troubleshooting, including both methods for a temporary "quick fix" and for more effective long-term solutions. The most important plant measurements to identify the source of the problem are listed. The various categories of problem are then described in turn; they include commissioning, start-up and shutdown, safety and environmental problems, underperformance, poor product quality, material handling and blockage, transient problems and mechanical breakdown. Some of the specific problems encountered with individual types of dryer are then described, with the aid of selected case studies.

It is intended to incorporate the basic problem-solving method into a simplified expert system, provisionally entitled DRYSOLVE, in the next couple of years. If this approach is successful, a program using a more detailed and rigorous methodology could be developed later.


Volume DRY XI Part 4 Energy Aspects.

Thermal drying is an extremely energy intensive operation. In many instances, dryers are operated unknowingly at efficiencies well below their potential, adding unnecessarily to drying costs. This report aims to give dryer users and manufacturers information on how to measure the efficiency of an existing dryer and on how to improve its performance. The measurement and analysis of heat and mass balances is covered in detail. A wide variety of drying systems is described by a series of modules which can be combined together as required. Schemes for reducing energy consumption are divided into two categories. First, there are those that require negligible or minor capital expenditure, such as good house keeping, reduction of the air supply, optimisation of production schedules and simple improvements to instrumentation and control. Secondly, there are those that need significant capital expenditure such as improved mechanical dewatering, heat recovery from exhaust gas and product, recycling of exhaust air and advanced instrumentation and control. The report also considers the much wider opportunities available with a new plant at the design stage, including dry rather than wet processing, pre-concentration by evaporation or mechanical dewatering, replacing water by a low latent heat organic solvent, dryer selection and the use of the Carver Greenfield process. The final chapter describes several potential technical developments which have yet to make a significant impact in industry, namely high temperature closed cycle heat pumps, open cycle heat pumps, vacuum flash evaporation and the use of "free" heat sources.