Analyzing and troubleshooting single-screw extruders
Prior extrusion books are based on barrel rotation physics. This is the first book that focuses on the actual physics of the process - screw rotation physics. In the first nine chapters, theories and math models are developed. Then, these models are used to solve actual commercial problems in the re...
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| Main Authors | , |
|---|---|
| Format | Electronic eBook |
| Language | English |
| Published |
Munich, Germany ; Cincinnati, Ohio :
Hanser Publishers,
[2021]
|
| Edition | 2nd edition. |
| Subjects | |
| Online Access | Full text |
| ISBN | 9781569907856 1569907854 9781569907849 |
| Physical Description | 1 online resource : illustrations |
Table of Contents:
- Intro
- Contents
- Preface
- Acknowledgements
- 1 Single-Screw Extrusion: Introduction and Troubleshooting
- 1.1 Organization of this Book
- 1.2 Troubleshooting Extrusion Processes
- 1.2.1 The Injection Molding Problem at Saturn
- 1.3 Introduction to Screw Geometry
- 1.3.1 Screw Geometric Quantitative Characteristics
- 1.4 Simple Flow Equations for the Metering Section
- 1.5 Example Calculations
- 1.5.1 Example 1: Calculation of Rotational and Pressure Flow Components
- 1.5.2 Example 2: Flow Calculations for a Properly Operating Extruder
- 1.5.3 Example 3: Flow Calculations for an Improperly Operating Extruder
- 1.5.4 Metering Channel Calculation Summary
- Nomenclature
- References
- 2 Polymer Materials
- 2.1 Introduction and History
- 2.1.1 History of Natural Polymers
- 2.1.2 The History of Synthetic Polymers
- 2.2 Characteristics of Synthetic Polymers
- 2.3 Structure Effects on Properties
- 2.3.1 Stereochemistry
- 2.3.2 Melting and Glass Transition Temperatures
- 2.3.3 Crystallinity
- 2.4 Polymer Production and Reaction Engineering
- 2.4.1 Condensation Reactions
- 2.4.2 Addition Reactions
- 2.5 Polymer Degradation
- 2.5.1 Ceiling Temperature
- 2.5.2 Degradation of Vinyl Polymers
- 2.5.3 Degradation of Condensation Polymers
- References
- 3 Introduction to Polymer Rheology for Extrusion
- 3.1 Introduction to the Deformation of Materials
- 3.2 Introduction to Basic Concepts of Molecular Size
- 3.2.1 Size Distribution Example
- 3.2.2 Molecular Weight Distributions for Polymers
- 3.3 Basic Rheology Concepts
- 3.4 Polymer Solution Viscosity and Polymer Molecular Weight
- 3.4.1 Sample Calculation of Solution Viscosity
- 3.5 Introduction to Viscoelasticity
- 3.6 Measurement of Polymer Viscosity
- 3.6.1 Capillary Rheometers
- 3.6.2 Cone and Plate Rheometers
- 3.6.3 Melt Index and Melt Flow Rate.
- 3.7 Viscosity of Polymers as Functions of Molecular Character, Temperature, and Pressure
- 3.8 Historical Models for Non-Newtonian Flow
- 3.9 Power Law and Viscosity Shear Rate Dependence
- 3.9.1 Shear Stress from Newtonian to Infinite Shear
- 3.9.2 Viscosity as a Function of Shear Rate
- 3.9.3 The Power Law and Process Dissipation
- 3.9.4 Viscosity, Shear Rate, and Dissipation
- 3.9.5 Percolation in Structured Systems
- 3.9.6 Tube Flow Data and Data Analysis
- 3.9.7 Dispersion Based Power Law Constant n
- 3.9.8 Rheological Implictions for Extrusion and Molding Processes
- Nomenclature
- References
- 4 Resin Physical Properties Related to Processing
- 4.1 Bulk Density and Compaction
- 4.1.1 Measurement of Bulk Density
- 4.1.2 Measuring the Compaction Characteristics of a Resin
- 4.2 Lateral Stress Ratio
- 4.2.1 Measuring the Lateral Stress Ratio
- 4.3 Stress at a Sliding Interface
- 4.3.1 The Screw Simulator and the Measurement of the Stress at the Interface
- 4.4 Melting Flux
- 4.5 Heat Capacity
- 4.6 Thermal Conductivity and Heat Transfer
- 4.7 Melt Density
- Nomenclature
- References
- 5 Solids Conveying
- 5.1 Description of the Solids Conveying Process
- 5.2 Literature Review of Smooth-Bore Solids Conveying Models
- 5.2.1 Darnell and Mol Model
- 5.2.2 Tadmor and Klein Model
- 5.2.3 Clarkson University Models
- 5.2.4 Hyun and Spalding Model
- 5.2.5 Moysey and Thompson Model
- 5.3 Modern Experimental Solids Conveying Devices
- 5.3.1 Solids Conveying Devices at Clarkson University
- 5.3.2 The Solids Conveying Device at Dow
- 5.4 Comparison of the Modified Campbell-Dontula Model with Experimental Data
- 5.4.1 Solids Conveying Example Calculation
- 5.5 Grooved Bore Solids Conveying
- 5.5.1 Grooved Barrel Solids Conveying Models
- 5.6 Solids Conveying Notes
- Nomenclature
- References
- 6 The Melting Process.
- 6.1 Compression Ratio and Compression Rate
- 6.2 The Melting Process
- 6.2.1 The Melting Process as a Function of Screw Geometry
- 6.2.2 Review of the Classical Literature
- 6.2.3 Reevaluation of the Tadmor and Klein Melting Data
- 6.3 Theory Development for Melting Using Screw Rotation Physics
- 6.3.1 Melting Model for a Conventional Transition Section Using Screw Rotation Physics
- 6.3.2 Melting Models for Barrier Screw Sections
- 6.4 Effect of Pressure on Melting Rate
- 6.5 One-Dimensional Melting
- 6.5.1 One-Dimensional Melting Model
- 6.6 Solid Bed Breakup
- 6.7 Melting Section Characteristics
- Nomenclature
- References
- 7 Fluid Flow in Metering Channels
- 7.1 Introduction to the Reference Frame
- 7.2 Laboratory Observations
- 7.3 Literature Survey
- 7.4 Development of Linearized Flow Analysis
- 7.4.1 Example Flow Calculation
- 7.5 Numerical Flow Evaluation
- 7.5.1 Simulation of a 500 mm Diameter Melt-Fed Extruder
- 7.5.2 Extrusion Variables and Errors
- 7.5.3 Corrections to Rotational Flow
- 7.5.4 Simulation of the 500 mm Diameter Extruder Using Fc
- 7.6 Frame Dependent Variables
- 7.6.1 Example Calculation of Energy Dissipation
- 7.7 Viscous Energy Dissipation and Temperature of the Resin in the Channel
- 7.7.1 Energy Dissipation and Channel Temperature for Screw Rotation
- 7.7.2 Energy Dissipation and Channel Temperature for Barrel Rotation
- 7.7.3 Temperature Increase Calculation Example for a Screw Pump
- 7.7.4 Heat Transfer Coefficients
- 7.7.5 Temperature Calculation Using a Control Volume Technique
- 7.7.6 Numerical Comparison of Temperatures for Screw and Barrel Rotations
- 7.8 Metering Section Characteristics
- Nomenclature
- References
- 8 Mixing Processes for Single-Screw Extruders
- 8.1 Common Mixing Operations for Single-Screw Extruders
- 8.1.1 Common Mixing Applications.
- 8.2 Dispersive and Distributive Mixing Processes
- 8.3 Fundamentals of Mixing
- 8.3.1 Measures of Mixing
- 8.3.2 Experimental Demonstration of Mixing
- 8.4 The Melting Process as the Primary Mechanism for Mixing
- 8.4.1 Experimental Analysis of the Melting and Mixing Capacity of a Screw
- 8.4.2 Mixing and Barrier-Flighted Melting Sections
- 8.5 Secondary Mixing Processes and Devices
- 8.5.1 Maddock-Style Mixers
- 8.5.2 Blister Ring Mixers
- 8.5.3 Spiral Dam Mixers
- 8.5.4 Pin-Type Mixers
- 8.5.5 Knob Mixers
- 8.5.6 Gear Mixers
- 8.5.7 Dynamic Mixers
- 8.5.8 Static Mixers
- 8.6 Mixing Using Natural Resins and Masterbatches
- 8.7 Mixing and Melting Performance as a Function of Flight Clearance
- 8.8 High Pressures During Melting and Agglomerates
- 8.9 Effect of Discharge Pressure on Mixing
- 8.10 Shear Refinement
- 8.11 Direct Compounding Using Single-Screw Extruders
- Nomenclature
- References
- 9 Scaling of Single-Screw Extrusion Processes
- 9.1 Scaling Rules
- 9.2 Engineering Design Method for Plasticating Screws
- 9.2.1 Process Analysis and Simulations
- 9.3 Scale-Up from a 40 mm Diameter Extruder to an 80 mm Diameter Machine for a PE Resin
- 9.4 Rate Increase for an 88.9 mm Diameter Extruder Running a HIPS Resin
- Nomenclature
- References
- 10 Introduction to Troubleshooting the Extrusion Process
- 10.1 The Troubleshooting Process
- 10.2 Hypothesis Setting and Problem Solving
- 10.2.1 Case Study for the Design of a New Resin
- 10.2.2 Case Study for a Surface Blemish
- 10.2.3 Case Study for a Profile Extrusion Process
- 10.3 Equipment and Tools Needed for Troubleshooting
- 10.3.1 Maddock Solidification Experiment
- 10.4 Common Mechanical Problems
- 10.4.1 Flight Clearance and Hard Facing
- 10.4.2 Barrel and Screw Alignment
- 10.4.3 Extruder Barrel Supports
- 10.4.4 First-Time Installation of a Screw.
- 10.4.5 Screw Breaks
- 10.4.6 Protection from High-Pressure Events
- 10.4.7 Gearbox Lubricating Oil
- 10.4.8 Particle Seals and Viscoseals
- 10.4.9 Screw Cleaning
- 10.5 Common Electrical and Sensor Problems
- 10.5.1 Thermocouples
- 10.5.2 Pressure Sensors
- 10.5.3 Electronic Filters and Noise
- 10.6 Motors and Drive Systems
- 10.6.1 Motor Efficiencies and Power Factors
- 10.7 Typical Screw Channel Dimensions
- 10.8 Common Calculations
- 10.8.1 Energy Dissipated by the Screw
- 10.8.2 Screw Geometry Indices
- 10.9 Barrel Temperature Optimization
- 10.10 Screw Temperature Profile
- 10.11 The Screw Manufacturing and Refurbishing Process
- 10.12 Injection-Molding Plasticators
- 10.12.1 Calculations for Injection-Molding Plasticators
- 10.13 New Equipment Installations
- 10.13.1 Case Study: A Large Diameter Extruder Purchase
- 10.13.2 Case Study: Extruder and Line Purchase for a New Product
- 10.13.3 A High-Density Foamed Sheet Product
- 10.13.4 Summary for New Equipment Installations
- Nomenclature
- References
- 11 Contamination in the Finished Product
- 11.1 Foreign Contaminants in the Extrudate
- 11.1.1 Melt Filtration
- 11.1.2 Metal Fragments in the Extrudate
- 11.1.3 Gas Bubbles in a New Sheet Line
- 11.2 Gels in Polyolefin Resins
- 11.2.1 Protocols for Gel Analysis
- 11.3 Resin Decomposition in Stagnant Regions of a Process
- 11.3.1 Transfer Lines
- 11.4 Improper Shutdown of Processing Equipment
- 11.5 Equipment Purging
- 11.6 Oxygen Exclusion at the Hopper
- 11.7 Flight Radii Size
- 11.8 Drying the Resin
- 11.9 Color Masterbatches
- 11.10 Case Studies for Extrusion Processes with Contamination in the Product
- 11.10.1 Intermittent Crosslinked Gels in a Film Product
- 11.10.2 Small Gels in an LLDPE Film Product
- 11.10.3 Degassing Holes in Blow-Molded Bottles.