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  • 1
    UID:
    almahu_9949697325702882
    Format: 1 online resource (881 pages)
    Edition: 1st ed.
    ISBN: 1-5231-4507-2 , 1-56990-838-9
    Content: Plastics production comprises the main process steps "synthesis (reaction)", "preparation/compounding" at the raw material manufacturer and compounder, and "processing" (shaping into semi-finished or finished products). In this handbook, the central middle step, preparation and compounding, is discussed. The preparation tasks include the removal of components, the incorporation of additives, and the change of particle size. Compounding is the incorporation of additives into a polymer or plastic. The process engineering fundamentals and the specific equipment and machines used are described. The specialist authors impart their knowledge from the fields of research, polymer production, and equipment/machine production with applications in plastics technology.
    Note: Intro -- The Authors -- In Memoriam -- Preface -- Contents -- PART A: Introduction to the Processing of Polymers -- 1 Introduction -- Klemens Kohlgrüber, Michael Bierdel -- 1.1 Plastics and Their Importance -- 1.2 Processing and Compounding -- 1.3 Recycling of Plastics -- 1.4 Guide to the Individual Chapters of this Book -- 2 Polymer Processing - Process Technology of Polymer Production -- Klemens Kohlgrüber -- 2.1 Introduction -- 2.2 Polymer Processing during the Polymer Synthesis in the Primary Production -- 2.3 Polymer Processing after the Polymer Production - Compounding -- 2.3.1 Main Temperature Window when Compounding for Finish Mixture -- 2.3.2 Mixing in the Extruder -- 2.3.3 Temperature and Time Limits for Compounding -- 2.3.4 Challenges when Compounding -- 2.3.5 Energy Requirement when Compounding -- 2.3.6 Range of Performance of Extruder -- 2.3.7 Throughput and Performance Density -- 2.3.8 Performance Density in the Melt Area -- 2.3.9 Energy Balance and Product Discharge Temperature -- 2.3.10 Static Mixers -- 2.3.11 Mixing Performance, Mixing Quality, Cross Mixing, Longitudinal Mixing -- 2.3.11.1 Mixing Performance -- 2.3.11.2 Mixing Performance and Mixing Quality -- 2.3.11.3 Cross and Longitudinal Mixing -- 2.3.11.4 Residence Time Distribution -- 2.3.11.5 Mean Residence Time -- PART B: Processing in Polymer Production -- 3 Devolatilizing Devices -- 3.1 Fundamentals of Devolatilization -- Heino Thiele -- 3.1.1 Phase Equilibrium -- 3.1.2 Macroscopic Mass and Energy Balance -- 3.1.3 Quantities Influencing the Change in Concentration -- 3.1.4 General Conclusions -- 3.2 Polymer Production and Degassing Tasks -- Klemens Kohlgrüber -- 3.2.1 General Challenges at the Degassing of Volatiles from Polymers -- 3.2.2 Special Features at the Degassing of Polymers with High Content of Volatiles and Limitation of Finish Degassing. , 3.3 Overview of Devices and Machines for Compounding with Polymer Degassing -- Klemens Kohlgrüber -- 3.3.1 Introduction -- 3.3.2 Devices with Rotating Components and Machines -- 3.4 Apparatus-Based Polymer Evaporation -- Klemens Kohlgrüber -- 3.4.1 Tube Evaporator -- 3.4.2 Process and Devices for Finish Degassing for Very Low Residual Contents in the Polymer -- 3.4.3 General Scheme of an Apparatus-Based Evaporation Stage -- 3.4.4 Product Quality -- 3.5 Degassing of Polymers in Purge Bins -- Harald Wilms, Hans Schneider -- 3.5.1 Introduction -- 3.5.2 Process Requirements for Degassing of Solids -- 3.5.3 Basics of Particle Degasssing -- 3.5.4 Determination of Degassing Process Parameters -- 3.5.4.1 Oven Tests -- 3.5.4.2 Batch Trials -- 3.5.4.3 Pilot Plant Tests -- 3.5.4.4 Criteria for the Gas Flow Rate for Degassing -- 3.5.5 Design Requirements for the Degassing Silo -- 3.5.6 Heating of Bulk Solids -- 3.5.7 Energy-Efficient Plant Concepts -- 3.5.8 Comparable Applications -- 3.5.9 Summary -- PART C: Processing after Polymer Production - Compounding -- 4 Requirements, Product Development, Additives, Sources of Faults -- 4.1 Compounding Requirements from the Compounder's Perspective -- Thomas Schuldt -- 4.1.1 Introduction -- 4.1.2 Economics -- 4.1.3 Technical Requirements along the Process Chain -- 4.1.3.1 Material Handling -- 4.1.3.2 Raw Material Pre-Treatment -- 4.1.3.3 Premixing -- 4.1.3.4 Extruder and Wear -- 4.1.3.5 Cooling and Pelletizing -- 4.1.3.6 Packaging -- 4.1.4 Quality Control -- 4.1.5 Environmental Aspects -- 4.1.6 Conclusions -- 4.2 Product Development -- Thomas Schuldt -- 4.2.1 Introduction -- 4.2.2 Types of Product Development -- 4.2.3 Building Blocks of Product Development -- 4.2.3.1 Equipment Technology -- 4.2.3.2 Process Technology -- 4.2.3.3 Formulation -- 4.2.4 Ingredients -- 4.2.4.1 Additives -- 4.2.4.2 Fillers -- 4.2.4.3 Pigments. , 4.2.5 Innovation -- 4.2.6 Quality Control -- 4.2.7 Scale-up -- 4.3 Additives for Polymers - From Polymer to Plastic -- Hermann Diem -- 4.3.1 Blends -- 4.3.1.1 Definition of Blends -- 4.3.1.2 Classification of Multi-Phase Systems -- 4.3.1.2.1 Polymer Blends -- 4.3.1.2.2 Dry Blends -- 4.3.2 Additives -- 4.3.2.1 Definition of Additives -- 4.3.2.2 Effects and Mode of Operation of the Additives -- 4.3.2.2.1 Plasticizers -- 4.3.2.2.2 Stabilizers -- 4.3.2.3 Incorporation of Additives into Polymers -- 4.3.3 Fillers -- 4.3.3.1 Definition of Fillers -- 4.3.3.2 Classification and Properties of Fillers -- 4.3.3.3 Aspect Ratio -- 4.4 Practical Examples Regarding Sources of Fault/Avoidance of Faults during Compounding -- Klemens Kohlgrüber -- 4.4.1 Black Specks -- 4.4.2 Sources at Dosing and Mixing -- 4.4.2.1 Demixing -- 4.4.2.2 Dosing System -- 4.4.2.3 Mixing of Polymer with Additives -- 4.4.3 Drive-Measurement Technique -- 4.4.4 Faults in Tests with Small Extruders for Scale-up Purposes -- 5 Compounding with Co-Rotating Twin-Screw Extruders -- 5.1 Introduction -- Klemens Kohlgrüber -- 5.1.1 Advantages of the Co-Rotating Twin-Screw Extruder -- 5.1.2 Disadvantages of the Co-Rotating Twin-Screw Extruder -- 5.1.3 Range of Services and Power Density of Co-Rotating Twin-Screw Extruders -- 5.1.4 Parameters in Dependence on the Diameter Ratio Da/Di -- 5.1.4.1 Strength and Throughput as a Function of Da/Di -- 5.1.4.2 Pressure and Power Characteristic as a Function of Da/Di -- 5.1.4.3 Maximum Product Volume -- 5.1.4.4 Inner Surface of the Housing to Maximum Product Space -- 5.1.4.5 Outlook -- 5.1.5 Special Types of Construction of the Co-Rotating Extruder -- 5.2 Tasks and Design of the Processing Zones of a Compounding Extruder -- Reiner Rudolf, Michael Bierdel -- 5.2.1 Melt Conveying Zone -- 5.2.2 Solids Conveying Zone -- 5.2.3 Plastification Zone. , 5.2.4 Distributive and Dispersive Mixing Zone -- 5.2.5 Devolatilization Zone -- 5.2.6 Pressure Build-up Zone -- 5.2.7 Complete Screw Configuration -- 5.2.8 Specific Energy Input -- 5.2.9 Residence Time Characteristics -- 5.3 Process and Screw Concepts for Machines with High Throughputs -- Frank Lechner -- 5.3.1 Development to High Torques, Volumes, and Rotations -- 5.3.2 Parameters and Process Limits of Co-Rotating Twin-Screw Kneaders -- 5.3.3 Process Length and Screw Development -- 5.3.4 Maximum Possible Screw Speed -- 5.3.5 Torque-Limited Processes -- 5.3.6 Volume-Limited Processes -- 5.3.7 Quality-Limited Processes -- 5.3.8 Process Concept for Economical Compounding -- 5.3.9 Outlook -- 5.4 Screw Designs for Highly Filled Polymers (and Dosing Strategies) -- Sebastian Fraas -- 5.4.1 Why Filler Compounds? -- 5.4.2 Typical Applications -- 5.4.3 Material-Specific Influencing Factors -- 5.4.3.1 Influence of Filler -- 5.4.3.1.1 Origin/Mining -- 5.4.3.1.2 Particle Size and Particle Size Distribution -- 5.4.3.1.3 Coating -- 5.4.3.1.4 Moisture Content -- 5.4.3.2 Polymer and Additives -- 5.4.4 Process Technology -- 5.4.4.1 Conveying Technology -- 5.4.4.2 Dosing Equipment -- 5.4.4.3 Downstream Equipment -- 5.4.4.4 Barrel Setup of an Extruder for Highly Filled Compounds -- 5.4.4.5 Screw Design -- 5.4.4.5.1 Melting Zone -- 5.4.4.5.2 Filler Addition and Wetting -- 5.4.4.5.3 Dispersion Zone -- 5.4.4.5.4 Vacuum and Discharge Zone -- 5.4.4.6 Entire System -- 5.5 Compounding of Natural Fiber Reinforced Plastics -- Dijan Iliew, Stephen Kroll, Andrea Siebert-Raths -- 5.5.1 Pre-Knowledge for the Processing of Natural Fibers -- 5.5.2 Design and Parameterization of the Process Unit of a Co-Rotating Twin-Screw Extruder -- 5.6 Fundamentals of Thermoplastic Foam Extrusion by Means of Parallel Twin-Screw Extruders -- Lukas Vogel. , 5.6.1 Definition and Characterization of Foams -- 5.6.2 Process Steps for Foam Extrusion -- 5.6.2.1 Provision of Thermoplastic Melts -- 5.6.2.2 Addition and Admixing of the Propellant (Blowing Agent) -- 5.6.2.3 Injecting the Blowing Agent and Conditioning of the Melt -- 5.6.2.4 Discharge of the Melt through the Die -- 5.6.2.5 Growth of Cells and Stabilization of the Foam Structure -- 5.6.3 System Components for Foam Extrusion -- 5.7 Screw Configurations -- Michael Bierdel -- 5.8 Materials, Coatings, Wear Technology -- Oliver Kayser -- 5.8.1 Requirements to the Components for Compounding -- 5.8.2 Materials and Heat Treatment -- 5.8.2.1 Tempering Steels and Nitriding Steels -- 5.8.2.2 Hot-Work Steels -- 5.8.2.3 Alloyed Cold-Work Steels -- 5.8.2.4 High-Speed Steels -- 5.8.3 Execution of Components of Twin-Screw Extruders -- 5.8.4 Process of Surface Layer Hardening -- 5.8.4.1 Wear Protection by Nitriding -- 5.8.4.2 Avoidance of Adhesive Wear due to Nitriding -- 5.8.4.3 Avoidance of Pitting Corrosion by Nitriding -- 5.8.4.4 Special Process for Maintaining Corrosion Protection -- 5.8.5 Wear Protection by Coatings -- 5.8.5.1 Hard Chromium -- 5.8.5.2 Chemical Nickel -- 5.8.5.3 Thin Layers of Hard Material -- 5.8.5.3.1 Physical Vapor Deposition -- 5.8.5.3.2 Chemical Vapor Deposition -- 5.8.6 Recommendations for Application -- 5.8.7 Summary and Outlook -- 6 Compounding and Polymer Processing with Different Extruder Types -- 6.1 Extruder Types - Introduction -- Klemens Kohlgrüber -- 6.1.1 Compounding and Processing with Different Extruder Types -- 6.1.2 Single-Screw Extruders -- 6.1.3 Gear Pumps -- 6.1.4 Co-Rotating Twin-Screw Extruders -- 6.1.5 Counter-Rotating Twin-Screw Extruders -- 6.1.6 Multi-Screw Extruders: RingExtruders and Planetary Roller Extruders -- 6.1.7 Non-Screw Extruders -- 6.1.8 High-Viscosity Reactors -- 6.2 Single-Screw Extruder. , Gregor Karrenberg. , In English.
    Additional Edition: Print version: Kohlgrüber, Klemens Plastics Compounding and Polymer Processing München : Hanser,c2021 ISBN 9781569908372
    Language: English
    Keywords: Handbooks and manuals. ; Handbooks and manuals. ; Handbooks and manuals.
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  • 2
    UID:
    almahu_9949225810002882
    Format: 1 online resource (xiii, 354 pages) : , illustrations
    Edition: 1st ed.
    ISBN: 3-446-43341-4
    Content: Provides basic engineering knowledge regarding twin-screw machines. The book lists the most important machine-technical requirements and provides examples based on actual practice. Better understanding of the processes is emphasized as this is a prerequisite for optimizing twin-screw designs and operating them efficiently.
    Note: Intro -- Preface -- Contents -- 1 Introduction -- 2 Historical Development of Co-RotatingTwin Screw Extruders -- 2.1 Introduction -- 2.2 Early Developments -- 2.3 Pioneering Period -- 2.4 New High Viscosity Technology with Co-RotatingExtruders -- 2.5 Special Developments from Bayer-Hochviskostechnik(High Viscosity Technology Group) -- 2.6 Developments after Licensing -- 2.7 Developments after Expiration of the Primary Patents -- 3 Rheological Properties of Polymer Melts -- 3.1 Introduction and Motivation -- 3.2 Classification of Rheological Behavior of Solidsand Fluids -- 3.3 Comparison of Viscous Fluid and Viscoelastic Fluid -- 3.4 Temperature Dependence of Shear Viscosity -- 3.5 Influence of Molecular Parameters on RheologicalProperties of Polymer Melts -- 3.6 Shear Flows -- 3.7 Extensional Flows -- 4 General Overview of the CompoundingProcess: Tasks, Selected Applications,and Process Zones -- 4.1 Compounding Tasks and Requirements -- 4.2 Tasks and Design of the Processing Zones of aCompounding Extruder -- 4.3 Characteristic Process Parameters -- 4.4 Process Examples -- 4.5 Technical Trends in Compounding -- 4.6 Symbols and Abbreviations -- 5 Geometry of the Co-Rotating Extruders:Conveying, and Kneading Elements -- 5.1 Introduction -- 5.2 The Fully Wiped Profile from Arcs -- 5.3 Geometric Design of Closely Intermeshing Profiles -- 5.4 Dimensions of Screw Elements with Clearances -- 5.5 Transition between Different Numbers of Threads -- 5.6 Calculation of a Screw Profile for Production Accordingto Planar Offset -- 5.7 Conveying Characteristics of Different Geometries -- 5.8 Kneading Elements -- 6 Modeling: Possibilities and Limitations -- 6.1 The Motivation for Modeling -- 6.2 Screw Design -- 6.3 Modeling Approaches -- 6.4 Model Dimensions -- 6.5 Extruder: 0-Dimensional -- 6.6 Extruder: 2-Dimensional -- 6.7 Extruder: 1-Dimensional. , 6.8 Extruder: 3-Dimensional -- 6.9 Simulation: Possibilities and Limitations -- 7 Pressure Generation and Energy Input inthe Melt -- 7.1 Operating Conditions of Conveying Screw Elements -- 7.2 Illustration of Dimensionless Groups -- 7.3 Calculation of the Back-Pressure Length -- 7.4 Efficiency during Pressure Generation -- 7.5 Example for the Design of a Pressure Build-Up Zone -- 7.6 Pressure and Energy behavior with Shear Thinning -- 8 Computational Fluid Dynamics -- 8.1 Why Computational Fluid Dynamics? -- 8.2 Workflow of a Computational Fluid Dynamics Process -- 8.3 Computational Examples -- 8.4 Conclusion and Outlook -- 9 Mixing and Dispersing: Principles -- 9.1 Introduction -- 9.2 Distributive Mixing -- 9.3 Dispersive Mixing -- 9.4 Determining the Mixing Quality -- 10 Degassing Polymer Melts with Co-RotatingTwin Screw Extruders -- 10.1 Requirements for Degassing -- 10.2 Function-Specific Design -- 10.3 Process Limits -- 10.4 Scale-Up -- 10.5 Process Examples -- 10.6 Conclusion -- 11 Simulation or Scale-Up -Alternatives for Extruder Layout? -- 11.1 Process Sections of the Compounding Extruder -- 11.2 Computation Possibilities for Discharge Parts -- 11.3 Scale-Up -- 12 Screw Elements for Co-rotating, CloselyIntermeshing, Twin-Screw Extruders -- 12.1 Design of the Screw Element -- 12.2 Combining Screw Elements -- 12.3 Screw Elements and How They Work -- 13 Overview of Patented Screw Elements -- 14 The ZSK Series and Applications in theChemical Industry and for Renewable RawMaterials -- 14.1 Development of High Torques, Volumesand Screw Speeds -- 14.2 Torque-Limited and Volume-Limited Throughputs -- 14.3 Process-Dependent Energy Requirement -- 14.4 Chemical and Pharmaceutical Applications -- 14.5 Applications for Renewable Raw Materials in thePlastic and Food Sectors -- 15 ZSK-NT the New Two-Stage ProcessingSystem for High Throughputs. , 15.1 Current Requirements for the Processing of Polyolefins -- 15.2 Two-stage Large-Scale Plants for the Processing ofBimodal Polyethylene -- 15.3 Quality Assessments for Bimodal Pipes -- 15.4 ZSK-NT Compared with Standard Technology -- 15.5 Design of Pressure Build-Up Zones -- 15.7 Outlook -- 15.8 Notation -- 16 Material Selection for Twin Screw ExtruderComponents in Contact with Resin -- 16.1 Introduction -- 16.2 What is Wear? -- 16.3 Wear in Operating Experience -- 16.4 Choice of Materials for Extruder Barrel and ScrewElements -- 17 Drive Units for Co-Rotating Twin-ScrewExtruders -- 17.1 Introduction -- 17.2 Drive Units for Small- to Medium-Size Co-RotatingTwin-Screw Extruders -- 17.3 Drive Units for Large Co-Rotating Extruders -- 17.4 Safety Clutches -- 17.5 Gearbox -- Index.
    Additional Edition: ISBN 3-446-41372-3
    Language: English
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  • 3
    UID:
    b3kat_BV046202901
    Format: XXVIII, 850 Seiten , Illustrationen, Diagramme , 25 cm
    ISBN: 9783446458321 , 3446458328
    Additional Edition: Erscheint auch als Online-Ausgabe ISBN 978-3-446-46079-9
    Language: German
    Subjects: Engineering , Physics
    RVK:
    RVK:
    RVK:
    RVK:
    Keywords: Polymere ; Aufbereitung ; Kunststoff ; Compoundierverfahren ; Kunststoff ; Aufbereitung ; Compoundierverfahren
    Author information: Rust, Harald 1949-2021
    Author information: Kohlgrüber, Klemens 1952-
    Author information: Bierdel, Michael
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  • 4
    UID:
    b3kat_BV047335018
    Format: 1 Online-Ressource (XXXI, 846 Seiten) , Illustrationen, Diagramme
    ISBN: 9781569908389
    Content: Plastics production comprises the main process steps "synthesis (reaction)", "preparation/compounding" at the raw material manufacturer and compounder, and "processing" (shaping into semi-finished or finished products). In this handbook, the central middle step, preparation and compounding, is discussed. The preparation tasks include the removal of components, the incorporation of additives, and the change of particle size. Compounding is the incorporation of additives into a polymer or plastic. The process engineering fundamentals and the specific equipment and machines used are described. The specialist authors impart their knowledge from the fields of research, polymer production, and equipment/machine production with applications in plastics technology. Dr. Klemens Kohlgrüber undertook a metalworking apprenticeship and completed further training as a mechanical engineer in Cologne. He studied mechanical engineering in Wuppertal, followed by a diploma and doctorate at RWTH Aachen University. From 1986 to 2015, he worked for Bayer AG, among other things as Head of High Viscosity, Mixing, and Reactor Technology. At the same time, he gave lectures for several years at the University of Dortmund for chemists in the master's program on polymer processing/preparation. For several years he was head of the High Viscosity Technology working group of the Forschungsgesellschaft Verfahrenstechnik (German Research Association for Process Engineering) and he is a former member of the Association of German Engineers (VDI) advisory board for plastics processing technology. Dr. Kohlgrüber also leads annual VDI seminars on extruders. Dr.-Ing. Michael Bierdel studied process engineering at the University of Stuttgart and received his doctorate in 2001. Since 2001 he has been working in research and development at Bayer Technology Services GmbH (Bayer AG), now Covestro Deutschland AG (Covestro AG), in the High Viscosity Technolo
    Additional Edition: Erscheint auch als Druck-Ausgabe ISBN 978-1-569-90837-2
    Language: German
    Subjects: Engineering , Physics
    RVK:
    RVK:
    Keywords: Kunststoffverarbeitung ; Polymercompound ; Kunststoff ; Aufbereitung ; Compoundierverfahren ; Polymere ; Kunststoff ; Aufbereitung ; Aufbereitung
    URL: Volltext  (URL des Erstveröffentlichers)
    Author information: Rust, Harald 1949-2021
    Author information: Kohlgrüber, Klemens 1952-
    Author information: Bierdel, Michael
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  • 5
    UID:
    b3kat_BV022887533
    Format: XIV, 367 S. , zahlr. Ill. und graph. Darst. , 25 cm
    ISBN: 9783446412521
    Language: German
    Subjects: Engineering
    RVK:
    RVK:
    Keywords: Doppelschneckenextruder ; Lehrbuch
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  • 6
    UID:
    kobvindex_ZLB13352982
    Format: XX, 123 Seiten , Ill., graph. Darst. , 21 cm
    ISBN: 3897227630
    Language: German
    Keywords: Betriebsverhalten ; Polyurethane ; Herstellung ; Gegenstrom-Injektions-Mischer ; Betriebsverhalten ; Mischgüte ; Polyurethane ; Herstellung ; Hochschulschrift
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  • 7
    UID:
    b3kat_BV023028380
    Format: XIII, 354 S. , zahlr. Ill. und graph. Darst. , 25 cm
    ISBN: 9783446413726 , 9781569904220
    Uniform Title: Gleichläufige Doppelschneckenextruder
    Additional Edition: Erscheint auch als Druck-Ausgabe ISBN 978-3-446-43341-0
    Language: English
    Subjects: Engineering
    RVK:
    Keywords: Doppelschneckenextruder ; Lehrbuch
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  • 8
    UID:
    b3kat_BV047639942
    Format: XXXI, 846 Seiten , Illustrationen, Diagramme , 25 cm
    ISBN: 9781569908372 , 1569908370
    Additional Edition: Erscheint auch als Online-Ausgabe ISBN 978-1-56990-838-9
    Language: German
    Subjects: Engineering , Physics
    RVK:
    RVK:
    Keywords: Kunststoffverarbeitung ; Polymercompound ; Kunststoff ; Aufbereitung ; Compoundierverfahren ; Polymere ; Kunststoff ; Aufbereitung ; Aufbereitung
    Author information: Rust, Harald 1949-2021
    Author information: Kohlgrüber, Klemens 1952-
    Author information: Bierdel, Michael
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  • 9
    UID:
    edoccha_9960073508802883
    Format: 1 online resource (xiii, 354 pages) : , illustrations
    Edition: 1st ed.
    ISBN: 3-446-43341-4
    Content: Provides basic engineering knowledge regarding twin-screw machines. The book lists the most important machine-technical requirements and provides examples based on actual practice. Better understanding of the processes is emphasized as this is a prerequisite for optimizing twin-screw designs and operating them efficiently.
    Note: Intro -- Preface -- Contents -- 1 Introduction -- 2 Historical Development of Co-RotatingTwin Screw Extruders -- 2.1 Introduction -- 2.2 Early Developments -- 2.3 Pioneering Period -- 2.4 New High Viscosity Technology with Co-RotatingExtruders -- 2.5 Special Developments from Bayer-Hochviskostechnik(High Viscosity Technology Group) -- 2.6 Developments after Licensing -- 2.7 Developments after Expiration of the Primary Patents -- 3 Rheological Properties of Polymer Melts -- 3.1 Introduction and Motivation -- 3.2 Classification of Rheological Behavior of Solidsand Fluids -- 3.3 Comparison of Viscous Fluid and Viscoelastic Fluid -- 3.4 Temperature Dependence of Shear Viscosity -- 3.5 Influence of Molecular Parameters on RheologicalProperties of Polymer Melts -- 3.6 Shear Flows -- 3.7 Extensional Flows -- 4 General Overview of the CompoundingProcess: Tasks, Selected Applications,and Process Zones -- 4.1 Compounding Tasks and Requirements -- 4.2 Tasks and Design of the Processing Zones of aCompounding Extruder -- 4.3 Characteristic Process Parameters -- 4.4 Process Examples -- 4.5 Technical Trends in Compounding -- 4.6 Symbols and Abbreviations -- 5 Geometry of the Co-Rotating Extruders:Conveying, and Kneading Elements -- 5.1 Introduction -- 5.2 The Fully Wiped Profile from Arcs -- 5.3 Geometric Design of Closely Intermeshing Profiles -- 5.4 Dimensions of Screw Elements with Clearances -- 5.5 Transition between Different Numbers of Threads -- 5.6 Calculation of a Screw Profile for Production Accordingto Planar Offset -- 5.7 Conveying Characteristics of Different Geometries -- 5.8 Kneading Elements -- 6 Modeling: Possibilities and Limitations -- 6.1 The Motivation for Modeling -- 6.2 Screw Design -- 6.3 Modeling Approaches -- 6.4 Model Dimensions -- 6.5 Extruder: 0-Dimensional -- 6.6 Extruder: 2-Dimensional -- 6.7 Extruder: 1-Dimensional. , 6.8 Extruder: 3-Dimensional -- 6.9 Simulation: Possibilities and Limitations -- 7 Pressure Generation and Energy Input inthe Melt -- 7.1 Operating Conditions of Conveying Screw Elements -- 7.2 Illustration of Dimensionless Groups -- 7.3 Calculation of the Back-Pressure Length -- 7.4 Efficiency during Pressure Generation -- 7.5 Example for the Design of a Pressure Build-Up Zone -- 7.6 Pressure and Energy behavior with Shear Thinning -- 8 Computational Fluid Dynamics -- 8.1 Why Computational Fluid Dynamics? -- 8.2 Workflow of a Computational Fluid Dynamics Process -- 8.3 Computational Examples -- 8.4 Conclusion and Outlook -- 9 Mixing and Dispersing: Principles -- 9.1 Introduction -- 9.2 Distributive Mixing -- 9.3 Dispersive Mixing -- 9.4 Determining the Mixing Quality -- 10 Degassing Polymer Melts with Co-RotatingTwin Screw Extruders -- 10.1 Requirements for Degassing -- 10.2 Function-Specific Design -- 10.3 Process Limits -- 10.4 Scale-Up -- 10.5 Process Examples -- 10.6 Conclusion -- 11 Simulation or Scale-Up -Alternatives for Extruder Layout? -- 11.1 Process Sections of the Compounding Extruder -- 11.2 Computation Possibilities for Discharge Parts -- 11.3 Scale-Up -- 12 Screw Elements for Co-rotating, CloselyIntermeshing, Twin-Screw Extruders -- 12.1 Design of the Screw Element -- 12.2 Combining Screw Elements -- 12.3 Screw Elements and How They Work -- 13 Overview of Patented Screw Elements -- 14 The ZSK Series and Applications in theChemical Industry and for Renewable RawMaterials -- 14.1 Development of High Torques, Volumesand Screw Speeds -- 14.2 Torque-Limited and Volume-Limited Throughputs -- 14.3 Process-Dependent Energy Requirement -- 14.4 Chemical and Pharmaceutical Applications -- 14.5 Applications for Renewable Raw Materials in thePlastic and Food Sectors -- 15 ZSK-NT the New Two-Stage ProcessingSystem for High Throughputs. , 15.1 Current Requirements for the Processing of Polyolefins -- 15.2 Two-stage Large-Scale Plants for the Processing ofBimodal Polyethylene -- 15.3 Quality Assessments for Bimodal Pipes -- 15.4 ZSK-NT Compared with Standard Technology -- 15.5 Design of Pressure Build-Up Zones -- 15.7 Outlook -- 15.8 Notation -- 16 Material Selection for Twin Screw ExtruderComponents in Contact with Resin -- 16.1 Introduction -- 16.2 What is Wear? -- 16.3 Wear in Operating Experience -- 16.4 Choice of Materials for Extruder Barrel and ScrewElements -- 17 Drive Units for Co-Rotating Twin-ScrewExtruders -- 17.1 Introduction -- 17.2 Drive Units for Small- to Medium-Size Co-RotatingTwin-Screw Extruders -- 17.3 Drive Units for Large Co-Rotating Extruders -- 17.4 Safety Clutches -- 17.5 Gearbox -- Index.
    Additional Edition: ISBN 3-446-41372-3
    Language: English
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  • 10
    UID:
    edocfu_9960073508802883
    Format: 1 online resource (xiii, 354 pages) : , illustrations
    Edition: 1st ed.
    ISBN: 3-446-43341-4
    Content: Provides basic engineering knowledge regarding twin-screw machines. The book lists the most important machine-technical requirements and provides examples based on actual practice. Better understanding of the processes is emphasized as this is a prerequisite for optimizing twin-screw designs and operating them efficiently.
    Note: Intro -- Preface -- Contents -- 1 Introduction -- 2 Historical Development of Co-RotatingTwin Screw Extruders -- 2.1 Introduction -- 2.2 Early Developments -- 2.3 Pioneering Period -- 2.4 New High Viscosity Technology with Co-RotatingExtruders -- 2.5 Special Developments from Bayer-Hochviskostechnik(High Viscosity Technology Group) -- 2.6 Developments after Licensing -- 2.7 Developments after Expiration of the Primary Patents -- 3 Rheological Properties of Polymer Melts -- 3.1 Introduction and Motivation -- 3.2 Classification of Rheological Behavior of Solidsand Fluids -- 3.3 Comparison of Viscous Fluid and Viscoelastic Fluid -- 3.4 Temperature Dependence of Shear Viscosity -- 3.5 Influence of Molecular Parameters on RheologicalProperties of Polymer Melts -- 3.6 Shear Flows -- 3.7 Extensional Flows -- 4 General Overview of the CompoundingProcess: Tasks, Selected Applications,and Process Zones -- 4.1 Compounding Tasks and Requirements -- 4.2 Tasks and Design of the Processing Zones of aCompounding Extruder -- 4.3 Characteristic Process Parameters -- 4.4 Process Examples -- 4.5 Technical Trends in Compounding -- 4.6 Symbols and Abbreviations -- 5 Geometry of the Co-Rotating Extruders:Conveying, and Kneading Elements -- 5.1 Introduction -- 5.2 The Fully Wiped Profile from Arcs -- 5.3 Geometric Design of Closely Intermeshing Profiles -- 5.4 Dimensions of Screw Elements with Clearances -- 5.5 Transition between Different Numbers of Threads -- 5.6 Calculation of a Screw Profile for Production Accordingto Planar Offset -- 5.7 Conveying Characteristics of Different Geometries -- 5.8 Kneading Elements -- 6 Modeling: Possibilities and Limitations -- 6.1 The Motivation for Modeling -- 6.2 Screw Design -- 6.3 Modeling Approaches -- 6.4 Model Dimensions -- 6.5 Extruder: 0-Dimensional -- 6.6 Extruder: 2-Dimensional -- 6.7 Extruder: 1-Dimensional. , 6.8 Extruder: 3-Dimensional -- 6.9 Simulation: Possibilities and Limitations -- 7 Pressure Generation and Energy Input inthe Melt -- 7.1 Operating Conditions of Conveying Screw Elements -- 7.2 Illustration of Dimensionless Groups -- 7.3 Calculation of the Back-Pressure Length -- 7.4 Efficiency during Pressure Generation -- 7.5 Example for the Design of a Pressure Build-Up Zone -- 7.6 Pressure and Energy behavior with Shear Thinning -- 8 Computational Fluid Dynamics -- 8.1 Why Computational Fluid Dynamics? -- 8.2 Workflow of a Computational Fluid Dynamics Process -- 8.3 Computational Examples -- 8.4 Conclusion and Outlook -- 9 Mixing and Dispersing: Principles -- 9.1 Introduction -- 9.2 Distributive Mixing -- 9.3 Dispersive Mixing -- 9.4 Determining the Mixing Quality -- 10 Degassing Polymer Melts with Co-RotatingTwin Screw Extruders -- 10.1 Requirements for Degassing -- 10.2 Function-Specific Design -- 10.3 Process Limits -- 10.4 Scale-Up -- 10.5 Process Examples -- 10.6 Conclusion -- 11 Simulation or Scale-Up -Alternatives for Extruder Layout? -- 11.1 Process Sections of the Compounding Extruder -- 11.2 Computation Possibilities for Discharge Parts -- 11.3 Scale-Up -- 12 Screw Elements for Co-rotating, CloselyIntermeshing, Twin-Screw Extruders -- 12.1 Design of the Screw Element -- 12.2 Combining Screw Elements -- 12.3 Screw Elements and How They Work -- 13 Overview of Patented Screw Elements -- 14 The ZSK Series and Applications in theChemical Industry and for Renewable RawMaterials -- 14.1 Development of High Torques, Volumesand Screw Speeds -- 14.2 Torque-Limited and Volume-Limited Throughputs -- 14.3 Process-Dependent Energy Requirement -- 14.4 Chemical and Pharmaceutical Applications -- 14.5 Applications for Renewable Raw Materials in thePlastic and Food Sectors -- 15 ZSK-NT the New Two-Stage ProcessingSystem for High Throughputs. , 15.1 Current Requirements for the Processing of Polyolefins -- 15.2 Two-stage Large-Scale Plants for the Processing ofBimodal Polyethylene -- 15.3 Quality Assessments for Bimodal Pipes -- 15.4 ZSK-NT Compared with Standard Technology -- 15.5 Design of Pressure Build-Up Zones -- 15.7 Outlook -- 15.8 Notation -- 16 Material Selection for Twin Screw ExtruderComponents in Contact with Resin -- 16.1 Introduction -- 16.2 What is Wear? -- 16.3 Wear in Operating Experience -- 16.4 Choice of Materials for Extruder Barrel and ScrewElements -- 17 Drive Units for Co-Rotating Twin-ScrewExtruders -- 17.1 Introduction -- 17.2 Drive Units for Small- to Medium-Size Co-RotatingTwin-Screw Extruders -- 17.3 Drive Units for Large Co-Rotating Extruders -- 17.4 Safety Clutches -- 17.5 Gearbox -- Index.
    Additional Edition: ISBN 3-446-41372-3
    Language: English
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