May
1999
Volume
76
Number
3
Pages
361
—
370
Authors
Andreas
Redl
,
1
,
2
Marie Hélène
Morel
,
1
Joëlle
Bonicel
,
1
Bruno
Vergnes
,
3
and
Stephane
Guilbert
1
Affiliations
Unité de Technologie des Céréales et des Agropolymères, ENSA.M-INRA, 2 place Viala, 34060 Montpellier Cedex 1, France.
Corresponding author. Phone: +33499612477. Fax: +33467522094. E-mail: REDL@ENSAM.INRA.FR
Ecole de Mines de Paris, CEMEF, UMR CNRS 7635, BP 207, 06904 Sophia Antipolis, France.
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RelatedArticle
Accepted January 5, 1999.
Abstract
ABSTRACT
Gluten-glycerol dough was extruded under a variety of processing conditions using a corotating self-wiping twin-screw extruder. Influence of feed rate, screw speed, and barrel temperature on processing parameters (die pressure, product temperature, residence time, specific energy) were examined. Use of flow modeling was successful for describing the evolution of the main flow parameters during processing. Rheological properties of extruded samples exhibited network-like behavior and were characterized and modeled by Cole-Cole distributions. Changes in molecular sizes of proteins during extrusion were measured by chromatography and appeared to be correlated to molecular size between network strands, as derived from the rheological properties of the materials obtained. Depending on operating conditions, extrudates presented very different surface aspects, ranging from very smooth-surfaced extrudates with high swell to completely broken extrudates. The results indicated that extrudate breakup was caused by increasing network density, and some gliadins may have acted as cross-linking agents. Increasing network density resulted in decreasing mobility of polymeric chains, and “protein melt” may no longer have been able to support the strain experienced during extrusion through the die. Increasing network density was reflected in increased plateau modulus and molecular size of protein aggregates. Increasing network structure appeared to be induced by the severity of the thermomechanical treatment, as indicated by specific mechanical energy input and maximum temperature reached.
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ArticleCopyright
© 1999 American Association of Cereal Chemists, Inc.