Influence of extrusion process conditions on starch film morphology
The conditions of extrusion process for food packaging are determinant on their morphology and, as consequence, on their functionality. The effect of the screw speed of a starch-glycerol system extruded at the same temperature profile was evaluated. The process at 80 rpm led to a material with the s...
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Academic Press
2017
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| 003 | AR-BaUEN | ||
| 005 | 20250423092400.0 | ||
| 008 | 190410s2017 xx ||||fo|||| 00| 0 eng|d | ||
| 024 | 7 | |2 scopus |a 2-s2.0-85020821884 | |
| 030 | |a LBWTA | ||
| 040 | |a Scopus |b spa |c AR-BaUEN |d AR-BaUEN | ||
| 100 | 1 | |a González-Seligra, P. | |
| 245 | 1 | 0 | |a Influence of extrusion process conditions on starch film morphology |
| 260 | |b Academic Press |c 2017 | ||
| 270 | 1 | 0 | |m Famá, L.; Universidad de Buenos Aires, Facultad de Ciencias Exactas y Naturales, Departamento de Física, Laboratorio de Polímeros y Materiales Compuestos (LPM&C), Instituto de Física de Buenos Aires (IFIBA-CONICET), Ciudad Universitaria (1428), Argentina; email: merfama@hotmail.com |
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| 506 | |2 openaire |e Política editorial | ||
| 520 | 3 | |a The conditions of extrusion process for food packaging are determinant on their morphology and, as consequence, on their functionality. The effect of the screw speed of a starch-glycerol system extruded at the same temperature profile was evaluated. The process at 80 rpm led to a material with the starch completely gelatinized, while the systems fabricated at 40 rpm and 120 rpm presented broken starch grains. The morphology and density of the broken grains depended on the screw speed. The material at 120 rpm showed broken grains with smaller size and lower concentration than that observed in the system at 40 rpm. After pressing at 120 rpm, the film formed (TPS120) resulted similar than that at 80 rpm (TPS80), while the film at 40 rpm (TPS40) kept some broken grains. TGA of the material obtained at 40 rpm showed more than one degradation process of the glycerol due to the inhomogeneous glycerol dispersion. DRX revealed more cristallinity in TPS40, being TPS120 the most amorphous. TPS80 had the highest strain at break while the others the higher modulus and stress at break. Water vapor permeability of TPS80 and TPS120 showed similar results and lower than TPS40. © 2017 |l eng | |
| 536 | |a Detalles de la financiación: PIP 2014? | ||
| 536 | |a Detalles de la financiación: Consejo Nacional de Investigaciones Científicas y Técnicas | ||
| 536 | |a Detalles de la financiación: 2012-1093 | ||
| 536 | |a Detalles de la financiación: Universidad de Buenos Aires | ||
| 536 | |a Detalles de la financiación: Secretaría de Ciencia y Técnica, Universidad de Buenos Aires | ||
| 536 | |a Detalles de la financiación: This work was supported by the following organizations: Agencia Nacional de Promoci?n Cient?fica y Tecnol?gica [ANPCyT 2012-1093], Consejo Nacional de Investigaciones Cient?ficas y T?cnicas [CONICET PIP 2014?2016 11220120100508CO, 2014?2016], and Universidad de Buenos Aires [UBACYT 2014?2017 20020130100495BA, 2014?2017]. | ||
| 593 | |a Universidad de Buenos Aires, Facultad de Ciencias Exactas y Naturales, Departamento de Física, Laboratorio de Polímeros y Materiales Compuestos (LPM&C), Instituto de Física de Buenos Aires (IFIBA-CONICET), Ciudad Universitaria (1428), Ciudad Autónoma de Buenos Aires, Argentina | ||
| 593 | |a Instituto de Investigación e Ingeniería Ambiental, CONICET, Universidad Nacional de San Martín, 25 de Mayo y Francia (1650), San Martín, Provincia de Buenos Aires, Argentina | ||
| 690 | 1 | 0 | |a EXTRUSION PROCESS CONDITIONS |
| 690 | 1 | 0 | |a MORPHOLOGY |
| 690 | 1 | 0 | |a PHYSICOCHEMICAL PROPERTIES |
| 690 | 1 | 0 | |a SCREW SPEED |
| 690 | 1 | 0 | |a STARCH |
| 690 | 1 | 0 | |a DISPERSIONS |
| 690 | 1 | 0 | |a GLYCEROL |
| 690 | 1 | 0 | |a MORPHOLOGY |
| 690 | 1 | 0 | |a SCREWS |
| 690 | 1 | 0 | |a STARCH |
| 690 | 1 | 0 | |a DEGRADATION PROCESS |
| 690 | 1 | 0 | |a EXTRUSION PROCESS |
| 690 | 1 | 0 | |a FOOD PACKAGING |
| 690 | 1 | 0 | |a PHYSICOCHEMICAL PROPERTY |
| 690 | 1 | 0 | |a SCREW SPEED |
| 690 | 1 | 0 | |a STRAIN AT BREAK |
| 690 | 1 | 0 | |a TEMPERATURE PROFILES |
| 690 | 1 | 0 | |a WATER VAPOR PERMEABILITY |
| 690 | 1 | 0 | |a EXTRUSION |
| 700 | 1 | |a Guz, L. | |
| 700 | 1 | |a Ochoa-Yepes, O. | |
| 700 | 1 | |a Goyanes, Silvia Nair | |
| 700 | 1 | |a Famá, L. | |
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