A Die Rotating System for Moderations of Extrusion Load and Pressure Drop Profiles for Molten PP and Wood/Polypropylene Composites in Extrusion Processes
被引:12
作者:
Intawong, Naret
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RMUTL, Fac Engn, Dept Ind Engn, Chiang Mai 50300, ThailandKMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, Thailand
Intawong, Naret
[2
]
Kantala, Chatchawan
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KMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, ThailandKMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, Thailand
Kantala, Chatchawan
[1
]
Lotaisong, Watit
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KMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, ThailandKMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, Thailand
Lotaisong, Watit
[1
]
Sombatsompop, Narongrit
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KMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, ThailandKMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, Thailand
Sombatsompop, Narongrit
[1
]
机构:
[1] KMUTT, Sch Energy Environm & Mat, Polymer Proc & Flow P PROF Grp, Bangkok 10140, Thailand
[2] RMUTL, Fac Engn, Dept Ind Engn, Chiang Mai 50300, Thailand
A die-rotating system was proposed in this work for moderations of extrusion forces and entrance pressure drop for molten polypropylene (PP) and wood/polypropylene (WPP) composites in a capillary rheometer and a single screw extruder. The effects of processing conditions and wood loading in PP were of our interests. The extrusion force and entrance pressure drop with and without the die rotating system were monitored in real-time. This was the first time that the die-rotating system was used for processing of highly viscous wood/polymer composite materials. It was found that the flow properties of the molten PP and WPP composites obeyed pseudoplastic non-Newtonian behavior. The behavior was more obvious at wood contents of above 6 wt % and in the capillary rhemeter. The rotation of the die could moderate the extrusion load by 60% and entrance pressure drop by 20% in the capillary rheometer, and the entrance pressure drop by 30% in the single screw extruder, especially at the conditions where the viscosities of the WPP and the extrusion rate were high. Greater fluctuations in entrance pressure drop caused by die rotation were observed in the single screw extruder. (C) 2010 Wiley Periodicals, Inc. J Appl Polym Sci 120: 1006-1016, 2011