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...

Full description

Saved in:
Bibliographic Details
Published inJournal of food science Vol. 69; no. 5; pp. E212 - E223
Main Authors Wang, L.J, Ganjyal, G.M, Jones, D.D, Weller, C.L, Hanna, M.A
Format Journal Article
LanguageEnglish
Published Oxford, UK Blackwell Publishing Ltd 01.06.2004
Institute of Food Technologists
Wiley Subscription Services, Inc
Subjects
Online AccessGet full text

Cover

Loading…
More Information
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.
Bibliography:istex:094A4E1B6132175FC0DB494318D539940B89797B
ark:/67375/WNG-LG1TPL1M-3
ArticleID:JFDSE212
ISSN:0022-1147
1750-3841
DOI:10.1111/j.1365-2621.2004.tb10712.x