1994
DOI: 10.1016/0260-8774(94)90185-6
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Relationships between residence time and process variables in a corotating twin-screw extruder

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Cited by 47 publications
(45 citation statements)
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“…When the screw speed is increased, the energy supplied by friction also increases because it is proportional to the velocity of the powder particles in the barrel. At the same time the quantity of heat transfer by conduction from the barrel wall decreases as the particle velocity increases, since the residence time of the product at the hot barrel wall decreases (2,38,39). Thus, the final dough temperatures would be dependent on the result of this combination effect, i.e.…”
Section: Effect Of Screw Speedmentioning
confidence: 93%
“…When the screw speed is increased, the energy supplied by friction also increases because it is proportional to the velocity of the powder particles in the barrel. At the same time the quantity of heat transfer by conduction from the barrel wall decreases as the particle velocity increases, since the residence time of the product at the hot barrel wall decreases (2,38,39). Thus, the final dough temperatures would be dependent on the result of this combination effect, i.e.…”
Section: Effect Of Screw Speedmentioning
confidence: 93%
“…On one hand, increasing screw speed and barrel temperature will introduce more energy to the material in the barrel, which would enhance the moisture evaporation at the die exit and hence increase ER. On the other hand, increasing screw speed will reduce the residence time of the material (Gogoi and Yam 1994), which could reduce the energy received by the material in the barrel, and therefore could result in lower ER. Sun and Muthukumarappan (2002) reported similar results when screw speed increased from 180 to 200 rpm and 220 rpm.…”
Section: Expansion Ratio (Er)mentioning
confidence: 98%
“…The expansion is influenced by physicochemical changes that occur during the extrusion, such as the gelatinization degree (Chinnaswamy;Bhattacharya, 1983;Feillet, 1975) and the molecular degradation of starch (Cai;Diosady, 1993;Gomez;Aguilera, 1983;Kirby et al, 1988). For this reason, the variables which influence the volume of the expanded are the extrusion temperature, the humidity, the rotation speed and the screw configuration, and array geometry Hanna, 1987;Colonna;Tayeb;Mercier, 1989;Gogoi;Yam, 1994; Owusu-Ansah; Van de Voort;Syanley, 1983). Higher temperatures in the 3 rd zone of the extruder might have provoked higher protein denaturation with consequential increase in the protein-protein and protein-starch interactions, harming the expansion.…”
Section: Resultsmentioning
confidence: 99%