Extruder Principles and Operation
Autor M. J. Stevens, J. A. Covasen Limba Engleză Paperback – 26 oct 2012
Preț: 1284.63 lei
Preț vechi: 1566.62 lei
-18%
Puncte Express: 1927
Carte tipărită la comandă
Livrare economică 14-28 iulie
Livrare prin curier în România Termenul estimat este afișat lângă disponibilitate.
Transport gratuit pentru acest produs Plată online sau ramburs, în funcție de opțiunile comenzii.
Retur gratuit în 14 zile Comandă securizată și suport în română.
Specificații
ISBN-13: 9789401042475
ISBN-10: 9401042470
Pagini: 512
Ilustrații: XI, 494 p.
Dimensiuni: 155 x 235 x 28 mm
Greutate: 0.77 kg
Ediția:Second Edition 1995
Editura: Springer
Locul publicării:Dordrecht, Netherlands
ISBN-10: 9401042470
Pagini: 512
Ilustrații: XI, 494 p.
Dimensiuni: 155 x 235 x 28 mm
Greutate: 0.77 kg
Ediția:Second Edition 1995
Editura: Springer
Locul publicării:Dordrecht, Netherlands
Public țintă
ResearchCuprins
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.