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Introduction | |
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Historical Development of the Co-Rotating Twin Screw | |
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Introduction | |
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Early Developments | |
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Basic Geometry | |
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Basic Patents | |
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Basic Patent of the Threaded Screw | |
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Basic Patent for Kneading Discs, DBP [16], USP [17], DBP [20] | |
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Basic Patent for Modular Design | |
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Pioneering Period | |
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Machine Development | |
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Use in Chemical Processes | |
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Licensing | |
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Recognition for R. Erdmenger | |
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New High Viscosity Technology with Co-Rotating Extruders | |
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Screw Machines in Process Engineering | |
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Similarity Theory for Screw Machinery | |
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Versatile High Viscosity Processes | |
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Special Developments from Bayer-Hochviskostechnik (High Viscosity Technology Group) | |
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Extended Kinematics, Profile Geometries | |
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Clearance Strategies | |
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Developments after Licensing | |
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Developments after Expiration of the Primary Patents | |
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Rheological Properties of Polymer Melts | |
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Introduction and Motivation | |
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Classification of Rheological Behavior of Solids and Fluids | |
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Comparison of Viscous and Viscoelastic Fluids | |
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Viscous Fluids | |
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Viscoelastic Fluids | |
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Temperature Dependence of Shear Viscosity | |
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Temperature Dependence for Semi-Crystalline Polymers | |
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Temperature Dependence for Amorphous Polymers | |
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Influence of Molecular Parameters on Rheological Properties of Polymer Melts | |
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Shear Flows | |
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Flow Profiles of Pressure-Driven Pipe Flow | |
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Flow Profiles of the Simple Drag Flow | |
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Extensional Flows | |
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General Overview of the Compounding Process: Tasks, Selected Applications, and Process Zones | |
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Compounding Tasks and Requirements | |
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Tasks and Design of the Processing Zones of a Compounding Extruder | |
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Intake Zone | |
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Plastification Zone | |
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Melt Conveying Zone | |
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Distributive Mixing Zone | |
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Dispersive Mixing Zone | |
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Devolatilization Zone | |
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Pressure Build-Up Zone | |
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Characteristic Process Parameters | |
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Specific Energy Input | |
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Residence Time Characteristics | |
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Process Examples | |
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Incorporation of Glass Fibers | |
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Incorporation of Fillers | |
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Production of Masterbatches | |
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Premix Process | |
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Split Feed Process | |
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Color Matching | |
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Coloring | |
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Technical Trends in Compounding | |
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Gear Element | |
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Ring Extruder | |
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TPE Production | |
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ZSK-NT Technology | |
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Injection Molding Compounder | |
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Symbols and Abbreviations | |
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Geometry of the Co-Rotating Extruders: Conveying, and Kneading Elements | |
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Introduction | |
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The Fully Wiped Profile from Arcs | |
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Geometric Design of Closely Intermeshing Profiles | |
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Dimensions of Screw Elements with Clearances | |
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Transition between Different Numbers of Threads | |
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Calculation of a Screw Profile for Production According to Longitudinal Offset | |
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Conveying Characteristics of Different Geometries | |
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Kneading Elements | |
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Modeling: Possibilities and Limitations | |
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The Motivation for Modeling | |
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Screw Design | |
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Modeling Approaches | |
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Model Dimensions | |
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Extruder: 0-Dimensional | |
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Whole Extruder | |
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Pumping Efficiency | |
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Extruder Section | |
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Extruder: 2-Dimensional | |
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Extruder: 1-Dimensional | |
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Extruder: 1-Dimensional, Extruder Section | |
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Extruder: 1-Dimensional, Whole Extruder | |
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Extruder: 3-Dimensional | |
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Model Depths and Results | |
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Extruder: 3-Dimensional, Fields | |
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Extruder: 3-Dimensional, Scalar Values | |
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Simulation: Possibilities and Limitations | |
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Pressure Generation and Energy Input in the Melt | |
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Operating States of Conveying Screw Elements | |
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Dimensionless Representation with Descriptive Impact | |
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Calculation of the Back-Pressure Length | |
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Efficiency during Pressure Generation | |
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Example for the Design of a Pressure Build-Up Zone | |
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Feed Behavior with Shear Thinning | |
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Computational Fluid Dynamics | |
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Why Computational Fluid Dynamics? | |
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Workflow of a Computational Fluid Dynamics Process | |
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Pre-Processing | |
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Flow Computation and Post-Processing | |
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Computational Examples | |
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Example 1 | |
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Example 2 | |
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Conclusion and Outlook | |
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Mixing and Dispersing: Principles | |
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Introduction | |
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Distributive Mixing | |
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Mixing in Laminar Flow | |
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Axial Mixing and Residence Time Distribution | |
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Dispersive Mixing | |
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Dispersion of Solid Particles | |
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Dispersion of Melts, Liquid Droplets, and Gas Bubbles | |
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Types of Loads and Frequency of Loads in an Extruder | |
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Determining the Mixing Quality | |
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Parameters | |
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Experimental Methods for Determining Mixing Quality and Residence Time Distribution | |
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Degassing Polymer Melts with Co-Rotating Twin Screw Extruders | |
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Requirements for Degassing | |
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Function-Specific Design | |
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Flash Vaporization | |
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Multi-Stage Vacuum | |
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Residual Degassing and Use of Stripping Agents | |
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Process Set-Up and Design of Degassing Zones | |
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Process Limits | |
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Scale-Up | |
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Process Examples | |
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Devolatilization of Solvents from LLDPE Melt Solutions | |
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Degassing Solvents from Synthetic Rubber (Styrene-Butadiene Compounds) | |
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Degassing Vinyl Acetate from LDPE/EVA Copolymer | |
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Degassing POM | |
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Degassing PC | |
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Degassing PES and PSU | |
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Degassing ABS | |
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Degassing Un-Dried PET | |
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Conclusion | |
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Simulation or Scale-Up - Alternatives for Extruder Layout? | |
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Process Sections of the Compounding Extruder | |
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Feed and Solid Conveying Section | |
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Plastification and Homogenizing Sections | |
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Devolatization and Discharge Sections | |
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Computation Possibilities in the Melt Phase | |
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Computation Possibilities for Discharge Parts | |
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Scale-Up | |
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Screw Elements for Co-Rotating, Closely Intermeshing, Twin-Screw Extruders | |
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Design of the Screw Element | |
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Combining Screw Elements | |
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Screw Elements and How They Work | |
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Conveying Elements | |
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Kneading Elements | |
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Backward-Pumping Elements | |
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Mixing Elements | |
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Special Elements | |
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Overview of Patented Screw Elements | |
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DE 813154, US 2670188 A | |
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DE 19947967A1, EP 1121238 B1, WO 2000020188 A1 | |
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US 1868671 A | |
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DE 10207145 B4, EP 1476290 A1, US 20050152214 A1 | |
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DE 940109 B, US 2814472 A | |
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US 3717330 A, DE 2128468 A1 | |
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DE 4118530 A1, EP 516936 B1, US 5338112 A | |
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US 4131371 A | |
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DE 3412258 A1, US 4824256 A | |
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DE 1180718 B, US 3254367 A | |
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US 3900187 A | |
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US 3216706 A | |
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EP 2131 A1 B2, JP 54072265 AA, US 4300839 A | |
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DE 19718292 A1, EP 875356 A1, US 6048088 A | |
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DE 4239220 A1 | |
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DE 1529919 A, US 3288077 A | |
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EP 330308 A1, US 5048971 A | |
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US 6783270 B1, WO 2002009919 A2 | |
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DE 10114727 B4, US 6974243 B2, WO 2002076707 A1 | |
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DE 4329612 A1, EP 641640 B1, US 5573332 A | |
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DE 19860256 A1, EP 1013402 A2, US 6179460 B1 | |
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DE 4134026 A1, EP 537450 B1, US 5318358 A | |
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DE 19706134 A1 | |
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WO 1998013189 A1, US 6022133 A, EP 934151 A1 | |
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WO 1999025537 A1, EP 1032492 A1 | |
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US 6116770 A, EP 1035960 A1, WO 2000020189 A1 | |
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DE 29901899 U1 | |
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US 6170975 B1, WO 2000047393 A1 | |
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DE 10150006 A1, EP 1434679 A1, US 7080935 B2 | |
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DE 4202821 C2, US 5267788 A, WO 9314921 A1 | |
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DE 3014643 A1, EP 37984 A1, US 4352568 A | |
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DE 2611908 A1, US 4162854 A | |
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WO 1995033608 A1, US 5487602 A, EP 764074 A1 | |
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DE 102004010553 A1 | |
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DE 4115591 A1, EP 513431 B1 | |
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The ZSK Series and Applications in the Chemical Industry and for Renewable Raw Materials | |
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Development of High Torques, Volumes and Screw Speeds | |
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Torque-Limited and Volume-Limited Throughputs | |
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Process-Dependent Energy Requirement | |
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Throughput-Energy Diagram | |
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High Torque for Glass Fiber Reinforcement of Plastics | |
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High Torque for Film Extrusion of Non-Dried PET or PLA | |
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Applications of Low Torques and High Volume Requirement | |
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Chemical and Pharmaceutical Applications | |
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Silicone Sealants | |
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Pressure-Sensitive Adhesives | |
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Ceramic Catalyst Carriers | |
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Insulating Films | |
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Battery Separator Films | |
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Metal and Ceramic Mixtures | |
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Pharmaceutical Mixtures | |
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Applications for Renewable Raw Materials in the Plastic and Food Sectors | |
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Composite Materials Made from Wood Fibers in Polyolefins | |
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Biodegradable Materials Made from Thermoplastic Starch and Polylactic Acid | |
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Extrusion Cooking of Cereals for Foodstuffs and Animal Feed | |
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Applications in the Confectionery Industry | |
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ZSK-NT the New Two-Stage Processing System for High Throughputs | |
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Current Requirements for the Processing of Polyolefins | |
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Two-stage Large-Scale Plants for the Processing of Bimodal Polyethylene | |
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Quality Assessments for Bimodal Pipes | |
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ZSK-NT Compared with the Standard Technology | |
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Design of Pressure Build-Up Zones | |
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Outlook | |
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Notation | |
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Material Selection for Twin Screw Extruder Components in Contact with Resin | |
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Introduction | |
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What is Wear? | |
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Wear in Operating Experience | |
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Choice of Materials for Extruder Barrel and Screw Elements | |
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Materials for Extruder Barrel | |
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Barrel Designs | |
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Material Variations | |
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Materials for Screw Elements | |
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Designs | |
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Material Variants | |
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Drive Units for Co-Rotating Twin-Screw Extruders | |
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Introduction | |
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Drive Units for Small- to Medium-Size Co-Rotating Twin-Screw Extruders | |
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Electric Motors | |
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Drive Configuration | |
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DC Drives | |
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Power Converters | |
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DC Motors | |
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Asynchronous Drives | |
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Frequency Converters | |
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Asynchronous Motors | |
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Network Feedback and EMC | |
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Motor Monitoring | |
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Torque Measurement | |
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Torque Measurement for Extruder Protection | |
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Torque Measurement for Scale-Up | |
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Bearing Currents | |
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Bearing Currents Caused by Asymmetry | |
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Bearing Currents Caused by Common Mode Voltage | |
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Bearing Currents Caused by Circular Flux | |
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Avoidable Sources of Error | |
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Corrective Measures | |
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Drive Units for Large Co-Rotating Extruders | |
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Drive Types | |
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Medium Voltage Asynchronous Motor | |
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Medium Voltage Synchronous Motors | |
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Fixed-Speed Drives | |
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Starting Aids | |
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Direct on-Line Starting | |
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Variable Speed Drives | |
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Frequency Converters | |
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Converter-Transformers | |
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Emergency Running Properties | |
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Safety Clutches | |
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Slip Clutches | |
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Mechanically Disengaging Clutches | |
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Gearbox | |
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Design | |
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Gear Teeth | |
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Bearing | |
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Lubrication | |