Finite element modeling of fluid flow, heat transfer, and melting of biomaterials in a single-screw extruder
A mathematical model was developed to simulate non-isothermal plug flow of granular starch in feed zone, melting in transition zone, and non-Newtonian melt flow in metering zone and die channel during single-screw extrusion processing. The maximum deviations between the predicted and experimental pr...
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Published in | Journal of food science Vol. 69; no. 5; pp. E212 - E223 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
Oxford, UK
Blackwell Publishing Ltd
01.06.2004
Institute of Food Technologists Wiley Subscription Services, Inc |
Subjects | |
Online Access | Get full text |
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Summary: | A mathematical model was developed to simulate non-isothermal plug flow of granular starch in feed zone, melting in transition zone, and non-Newtonian melt flow in metering zone and die channel during single-screw extrusion processing. The maximum deviations between the predicted and experimental pressure at the die entrance, product temperature at the die entrance, and minimum residence time were about 20%, 2.5%, and 8%, respectively, of the measured values when the barrel temperatures were 50 degrees C in the feed zone and 120 degrees C in the rest zones. The deviations were within 40%, 4%, and 15%, respectively, of the measured values when the barrel temperatures were 50 degrees C in the feed zone and 140 degrees C in the rest zones. Simulations were carried out to investigate the operating characteristics of an extruder, the melting degree, and profiles of pressure and bulk temperature during extrusion. |
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Bibliography: | istex:094A4E1B6132175FC0DB494318D539940B89797B ark:/67375/WNG-LG1TPL1M-3 ArticleID:JFDSE212 |
ISSN: | 0022-1147 1750-3841 |
DOI: | 10.1111/j.1365-2621.2004.tb10712.x |