This text is concerned with melt processing of thermoplastics and rubbers by means of the screw extruder. It is intended to bridge the gap between the theoretical performance of equipment primarily concerned with numerical design and the practical experience of the operator. Theoretical discussions generally give scant attention to practical aspects such as the conflict between productivity and product quality. The book opens with a description of the processes based on melt extrusions, with an emphasis on their differing requirements from the extruder, followed by a summary of flow and thermal properties relevant to extrusion. The principles of output and energy balance are then developed in a simplified form which is sufficiently accurate for most operational purposes, whilst retaining algebraic equations from which the effects of operational changes can be seen. The overall performance of the single-screw extruder is studied in terms of the separate effects of each controlled variable, the polymer properties and the screw design, followed by a tabulation of the various operational strategies to obtain a desired effect.The principles of operating twin-screw extruders are also examined in relation to screw geometry, and considerations of stability and product quality are followed by suggested control limits for specific processes. Practical information is given on start-up trials, scale-up, product changing, dismantling and cleaning. This book should be of interest to production/development technologists and engineers, quality control managers, plant design engineers, research technologists in plastics and rubber processing companies, and lecturers, researchers and postgraduates in materials processing in universities and technical colleges.
1 Introduction.- 1.1 Scope and limitations.- 1.2 Method.- 2 Practical extrusion processes and their requirements.- 2.1 Shaping processes and their requirements.- 2.2 Other applications and their requirements.- 3 Flow behaviour relevant to extrusion.- 3.1 Viscosity.- 3.2 Shear flow.- 3.3 Extensional flow.- 3.4 Elastic effects.- 3.5 Measurement of viscosity and elasticity.- 4 Thermal and energy properties in processing.- 4.1 Thermal properties.- 4.2 Thermal conduction.- 4.3 Non-isothermal flow and heat transfer.- 4.4 Mixing.- 5 Extrusion dies.- 5.1 Introduction.- 5.2 Factors influencing the performance of an extrusion die.- 5.3 Extrusion dies for some profiles.- 5.4 General principles of die design.- 5.5 Specific aspects of die design.- 5.6 Operational strategies for problem-solving.- 6 Principles of melt flow in single-screw extruders.- 6.1 Functions of the extruder.- 6.2 Derivation of flow equation.- 6.3 Leakage flow.- 6.4 Output equations and longitudinal pressure profiles for common screw types.- 6.5 Graphical representation of output for screw/die combinations, including venting.- 6.6 Output corrections.- 6.7 Pseudoplastic flow.- 6.8 Non-isothermal flow.- 7 Solids conveying and melting in single-screw extruders.- 7.1 The relevance of solids conveying and melting.- 7.2 Phenomenological description of solids conveying and melting.- 7.3 Theoretical analysis.- 8 Principles of energy balance.- 8.1 Energy balance and efficiency.- 8.2 Power consumption in the screw: Newtonian isothermal case.- 8.3 Pseudoplastic isothermal approximation.- 8.4 Power in non-isothermal flow.- 8.5 Effect of variables on energy balance.- 9 Operation of single-screw extruders.- 9.1 Overall performance of the screw.- 9.2 Effects of controlled variables.- 9.3 Polymer properties.- 9.4 Screw design.-9.5 Operational strategies.- 10 Twin-screw extruders.- 10.1 Non-intermeshing screws.- 10.2 Partial intermeshing.- 10.3 Full intermeshing: counterrotation.- 10.4 Full intermeshing: corotation.- 10.5 Comparison of machine types.- 11 Extruder operation as part of a total process.- 11.1 Quality.- 11.2 Stability.- 11.3 Shear history.- 11.4 Control.- 11.5 Scale-up.- 12 Practical extruder operation.- 12.1 Steady operation.- 12.2 Colour and grade changing.- 12.3 Start-up and shut-down.- 12.4 Dismantling and cleaning.- 12.5 Waste recovery.- 13 Application to the individual machine.- Appendices.- A Properties of polymers for heat and flow.- B Derivations of flow and pressure.- B.l Alternative derivation of flow equation.- B.2 Estimation of leakage flows.- B.3 Longitudinal pressure profiles.- B.4 Pressure gradients in a stepped screw.- C Energy consumption and energy balance.- C.l Experimental determination of energy balance.- C.2 Derivation of power absorbed in screw.- C.3 Heat flows in melt pumping section.- C.4 Distribution of shear heating and transverse circulation.- C.5 Temperature variation in the flight clearance.- D Stability of melt pumping section.- E List of tables.- References.