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Tubing Extrusion of a Fluoropolymer Melt

机译:含氟聚合物熔体的管材挤出

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摘要

The tubing extrusion-forming process of a fluoropolymer (FEP) melt was studied both experimentally and numerically. The flow behaviour of a FEP resin was determined by using a tubular die used in industrial-scale operations and these data were compared with simulation results using (i) a viscous model (Cross) and (ii) a viscoelastic one (the Kaye-Bernstein, Kearsley, Zapas / Papanastasiou, Scriven, Macos-ko or K-BKZ/PSM model) in order to assess the viscoelastic effects. In all simulations, compressibility, thermal and pressure effects on viscosity were taken into account. It was found that the viscoelastic results for the pressure, and hence the stresses at the wall, were always higher than the viscous results. Both were higher than the experimental results. A quadratic slip model plus viscoelasticity was found necessary to reproduce the experiments. The smooth flow curves resulting from this industrial tubular-coating die are a further manifestation that this is an appropriate design for coating fluoropolymers at very high apparent shear rates, exceeding 5000 s~(-1).
机译:对含氟聚合物(FEP)熔体的管材挤出成型工艺进行了实验和数值研究。 FEP树脂的流动性能是通过使用工业规模操作中使用的管状模具确定的,并将这些数据与使用以下模拟结果进行比较:(i)粘性模型(十字)和(ii)粘弹性模型(Kaye-Bernstein ,Kearsley,Zapas / Papanastasiou,Scriven,Macos-ko或K-BKZ / PSM模型)以评估粘弹性效应。在所有模拟中,均考虑了可压缩性,热和压力对粘度的影响。已发现,压力的粘弹性结果以及壁上的应力始终高于粘性结果。两者均高于实验结果。发现二次滑动模型加上粘弹性是重现实验所必需的。由该工业管状涂布模具产生的平滑流动曲线进一步表明,这是用于以非常高的表观剪切速率(超过5000 s〜(-1))涂布含氟聚合物的合适设计。

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