1998
DOI: 10.1002/pen.10348
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A global computer software for polymer flows in corotating twin screw extruders

Abstract: International audienceA global computation model for self-wiping corotating twin screw extruders is proposed. Based on a 1D approximated approach, it has been validated by comparison with experimentation and more sophisticated numerical models. It allows one to obtain, for any screw profile including left-and right-handed screw elements and kneading discs, the profile along the screws of the main flow variables, such as pressure, mean temperature, residence time, and filling ratio. Owing to the approximations … Show more

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Cited by 206 publications
(181 citation statements)
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“…The chosen rotation speeds are set to 300, 800 and 1200 rpm. These screw rotation speeds from 300 to 1200 rotations per minute correspond to shear rates ranging from 220 to 750 s -1 calculated thanks to Ludovic software [27] . The extrusion temperature and the feed rate (Q) are 200°C and 3 kg/h, respectively.…”
Section: Preparation Of Traced Blendsmentioning
confidence: 99%
“…The chosen rotation speeds are set to 300, 800 and 1200 rpm. These screw rotation speeds from 300 to 1200 rotations per minute correspond to shear rates ranging from 220 to 750 s -1 calculated thanks to Ludovic software [27] . The extrusion temperature and the feed rate (Q) are 200°C and 3 kg/h, respectively.…”
Section: Preparation Of Traced Blendsmentioning
confidence: 99%
“…linked by the relation F R = A × (Q/n) (Vergnes et al, 1998), where A is a constant value depending on the extruder geometry and the screw profile that were kept the same for all the study. Actually, if the amount of matter introduced in the machine became bigger, it was compensated by lower residence time along the screws due to a faster screw rotation.…”
Section: Composites Processingmentioning
confidence: 99%
“…For that various types of plasticizers such as glycerol, water, urea formamide etc are used during the formulation. The characteristics of mechanical work and flow (temperature, pressure, residence time, energy) during the preparation of TPS are known and modeled [Agassant et al, 1996, Vergnes et al, 1998]. A specific mechanical energy (SME) higher than 300kJ/g is necessary to achieve a complete destructuration of starch granules.…”
Section: Fabrication Of Thermoplastic Starchmentioning
confidence: 99%
“…The changes observed over time are due to several concurrent factors: reduction in water content [Van Soest et al, 1996 (b); Van Soest et al, 1996 (a)], increased Tg and crystallinity. Ageing causes reorientation and/or crystallization of molecules of amylose and amylopectin [Vergnes et al, 1998]. The crystallites acting as physical nodes, generate as stress concentrations and thus weaken the material [Van Soest et al, 1996 (b)].…”
Section: Mechanical Behaviormentioning
confidence: 99%