
Troubleshooting the Extrusion Process
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ISNI: 0000 0001 1876 3581
Content
- Intro
- Contents
- Acknowledgments
- Preface
- List of Acronyms
- 1 Requirements for Efficient Troubleshooting
- 1.1 Instrumentation
- 1.2 Understanding the Extrusion Process
- 1.3 Collection and Analysis of Historical Data (Time Line)
- 1.4 Team Building
- 1.5 Condition of the Equipment
- 1.6 Information about the Feed Stock
- 1.7 Problem-Solving Techniques
- 1.8 Collection and Interpretation of Extrusion Process Data
- 1.8.1 Introduction
- 1.8.2 Vital Signs of the Extrusion Process
- 1.8.2.1 Melt Pressure
- 1.8.2.2 Melt Temperature
- 1.8.2.3 Training
- 1.8.3 Conclusions
- 2 Tools for Troubleshooting
- 2.1 Temperature Measurement Devices
- 2.2 Data Acquisition Systems
- 2.2.1 Portable Data Collectors/Machine Analyzers
- 2.2.2 Fixed-Station Data Acquisition Systems
- 2.3 Light Microscopy
- 2.4 Thermochromic Materials
- 2.5 Thermal Analysis, IR Spectroscopy, and Rheometry
- 2.5.1 Differential Thermal Analysis and Differential Scanning Calorimetry
- 2.5.2 Thermogravimetric Analysis
- 2.5.3 Fourier Transform Infrared Spectroscopy
- 2.5.4 Thermomechanical Analysis
- 2.5.5 Torque Rheometry
- 2.5.6 High Pressure Capillary Rheometry
- 2.5.7 Rotational Rheometry
- 2.5.8 Other Thermal Characterization Techniques
- 2.6 Miscellaneous Tools
- 2.6.1 Infrared Thermography
- 2.6.2 The Smartphone
- 2.6.3 Power Measurements
- 3 Systematic Troubleshooting
- 3.1 Upsets versus Development Problems
- 3.2 Machine-Related Problems
- 3.2.1 The Drive System
- 3.2.2 The Feed System
- 3.2.3 The Heating and Cooling System
- 3.2.4 How Screw Design Can Affect Extruder Performance
- 3.2.5 Wear Problems
- 3.2.5.1 Wear Mechanisms
- 3.2.5.2 Test Methods for Wear
- 3.2.5.3 Causes of Wear
- 3.2.5.4 Solutions to Wear Problems
- 3.2.5.5 Rebuilding Worn Screws and Barrels
- 3.2.6 Screw Binding
- 3.2.6.1 Extrusion of Fluoropolymers
- 3.2.6.2 The Mechanics of Screw Binding
- 3.2.6.3 Changes in Clearance Due to Temperature Differences
- 3.2.6.4 Analysis of Temperature Distribution in Extruder Screws
- 3.2.6.5 Change in Clearance Due to Compressive Load
- 3.2.6.6 Results from Analysis
- 3.3 Polymer Degradation
- 3.3.1 Types of Degradation
- 3.3.1.1 Thermal Degradation
- 3.3.1.2 Mechanical Degradation
- 3.3.1.3 Chemical Degradation
- 3.3.2 Degradation in Extrusion
- 3.3.2.1 Residence Time Distribution
- 3.3.2.2 Temperature Distribution Simple Calculations
- 3.3.2.3 Temperature Distribution Numerical Calculations
- 3.3.2.4 Reducing Degradation
- 3.4 Extrusion Instabilities
- 3.4.1 Frequency of Instability
- 3.4.1.1 High-Frequency Instabilities
- 3.4.1.2 Screw Frequency Instabilities
- 3.4.1.3 Low-Frequency Instabilities
- 3.4.1.4 Very Slow Fluctuations
- 3.4.1.5 Random Fluctuations
- 3.4.2 Functional Instabilities
- 3.4.2.1 Solids-Conveying Instabilities
- 3.4.2.2 Plasticating Instabilities
- 3.4.2.3 Melt-Conveying Instabilities
- 3.4.2.4 Devolatilization Instabilities
- 3.4.2.5 Mixing Related Instabilities
- 3.4.2.6 Distributive Mixing Sections
- 3.4.2.7 Dispersive Mixing Sections
- 3.4.2.8 Solving Mixing Problems
- 3.4.2.9 Melt Temperature Variation
- 3.4.3 Solving Extrusion Instabilities
- 3.5 Air Entrapment
- 3.6 Gel Problems
- 3.6.1 Measuring Gels
- 3.6.2 Gels Created in the Extrusion Process
- 3.6.3 Removing Gels Produced in Polymerization
- 3.7 Die-Flow Problems
- 3.7.1 Melt Fracture
- 3.7.2 Die-Lip Buildup ("Die Drool")
- 3.7.3 V- or W-Patterns
- 3.7.4 Specks and Discoloration
- 3.7.5 Lines in Extruded Product
- 3.7.5.1 Weld Lines
- 3.7.6 Optical and Appearance Properties
- 4 Case Studies
- 4.1 Film Coextrusion - Degradation in the Middle Layer
- 4.1.1 Description of the Problem
- 4.1.2 Analysis of the Problem
- 4.1.3 Solution
- 4.2 Film Coextrusion with Interfacial Problems
- 4.2.1 Description of the Problem
- 4.2.2 Analysis of the Problem
- 4.2.3 Solution
- 4.3 Lines in the Extruded Film
- 4.3.1 Description of the Problem
- 4.3.2 Analysis of the Problem
- 4.3.3 Solution
- 4.4 Color Variation in Polypropylene Carpet Fiber
- 4.4.1 Description of the Problem
- 4.4.2 Analysis of the Problem
- 4.4.3 Solution
- 4.5 Plastic Film with Poor Transparency
- 4.5.1 Description of the Problem
- 4.5.2 Analysis of the Problem
- 4.5.3 Solution
- 4.6 Wear Problem in Film Extrusion
- 4.6.1 Description of the Problem
- 4.6.2 Solution
- 4.7 Multilayer Film - Several Appearance Problems
- 4.7.1 Description of the Problem
- 4.7.2 Analysis of the Problem
- 4.7.3 Solution
- 4.8 Dispersion Problem in a High-Density Polyethylene Bottle
- 4.8.1 Description of the Problem
- 4.8.2 Analysis of the Problem
- 4.8.3 Solution
- 4.9 Polymer Degradation
- 4.9.1 Description of the Problem
- 4.9.2 Analysis of the Problem
- 4.9.3 Solution
- 4.10 Heat-Sealing Problems in a Coextruded Film
- 4.10.1 Description of the Problem
- 4.10.2 Analysis of the Problem
- 4.10.3 Solution
- 4.11 Output Problem in a Blown Film Line
- 4.11.1 Description of the Problem
- 4.11.2 Analysis of the Problem
- 4.11.3 Solution
- 4.12 Masterbatch Selection
- 4.12.1 Description of the Problem
- 4.12.2 Analysis of the Problem
- 4.12.3 Solution
- 4.13 Pipe Extrusion Problem
- 4.13.1 Description of the Problem
- 4.13.2 Analysis of the Problem
- 4.13.3 Solution
- 4.14 Gel Formation in a Coextruded Film
- 4.14.1 Description of the Problem
- 4.14.2 Analysis of the Problem
- 4.14.3 Solution
- 4.15 Agglomerates and Grammage Variation in a PP Sheet
- 4.15.1 Description of the Problem
- 4.15.2 Analysis of the Problem
- 4.15.3 Solution
- 4.16 Insufficient Melting and Mixing in a Plasticating Unit
- 4.16.1 Description of the Problem
- 4.16.2 Analysis of the Problem
- 4.16.3 Solution
- 4.17 High Melt Temperature and Insufficient Output in Coextrusion
- 4.17.1 Description of the Problem
- 4.17.2 Analysis of the Problem
- 4.17.3 Solution
- 4.18 Deficient Solids Conveying and Dispersion
- 4.18.1 Description of the Problem
- 4.18.2 Analysis of the Problem
- 4.18.3 Solution
- 4.19 Instability of Formation at the Die
- 4.19.1 Description of the Problem
- 4.19.2 Analysis of the Problem
- 4.19.3 Solution
- 4.20 Intermittent Pumping in a Vented Extruder
- 4.20.1 Description of the Problem
- 4.20.2 Analysis of the Problem
- 4.20.3 Solution
- 4.21 Melt Fracture or Sharkskin in m-PE
- 4.21.1 Description of the Problem
- 4.21.2 Analysis of the Problem
- 4.21.3 Solution
- 4.22 Scale-up of LLDPE Single Screw Extruder
- 4.22.1 Description of the Problem
- 4.22.2 Analysis of the Problem
- 4.22.3 Solution
- 4.23 Non-homogeneous Melt in Blow Molding
- 4.23.1 Description of the Problem
- 4.23.2 Analysis of the Problem
- 4.23.3 Solution
- 4.24 High Melt Temperature in Sheet Extrusion
- 4.25 Gear Pump Speed Variation in Sheet Extrusion
- 4.26 Melt Temperature Variation in Tubing Extrusion
- 4.27 Black Specks in Tubing Extrusion
- 4.28 Mechanical Degradation in TPE Extrusion
- 4.29 Degradation in a Long Adapter
- 4.30 Shrink Voids in Rod Extrusion
- 4.31 Improper Preheating of Extruders
- Appendix 1: Systematic Problem Solving
- Appendix 2: Machine Troubleshooting and Maintenance
- A2.1 Check the Oil
- A2.2 Unusual Noises
- A2.3 Vibration Monitoring
- A2.4 Drive Motors and Belts
- A2.5 Spare Parts
- A2.6 Screw and Barrel
- A2.7 Extruder Maintenance Checklist
- Appendix 3: Extruder Barrel Temperatures
- A3.1 Setting Extruder Barrel Temperatures
- A3.2 Extruder Barrel Temperature Profile Optimization
- A3.2.1 Introduction
- A3.2.2 Facts about Barrel Temperature Profile (BTP)
- A3.2.3 Typical Process Temperatures for Different Plastics
- A3.2.4 Guidelines and Considerations for Setting Barrel Temperatures
- A3.2.5 BTP Optimization by Design of Experiments (DOE)
- A3.2.6 BTP Optimization by One-at-a-Time Experiments (OTE)
- A3.2.7 Dynamic BTP Optimization
- A3.2.8 Other Studies on Optimization of Extruder Barrel Temperature Profiles
- A3.2.9 Conclusions
- Appendix 4: Process Signal Analysis Using Fast Fourier Transform
- References
- Index
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