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PROCEDE D'EXTRUSION ET APPAREIL POUR LA MISE EN PRATIQUE DE CELUI-CI

机译:相同程序的挤出过程和装置

摘要

1370355 Extruding laminar plastics LEESONA CORP 8 Sept 1971 [9 Sept 1970] 41948/71 Heading B5A At least two different thermoplastics from different heated screw extrusion sources are combined in layers I, B, Fig. 5, parallel to the sides of the rectangular, e.g. square passage, of a die adapter, from which the layers are delivered to the outlet slot of a flat film die to be extruded as a laminate in which each layer, Fig. 6, is of substantially uniform thickness across the full width of the extrusion, compared to the variation experienced at the edges, Fig. 8 (not shown), when the layers are combined in a circular passage. The extruded film is drawn from the die by a vertical three roll stack. The layers of the extrusion may comprise low or medium and high density polyethylene, e.g. for shrink film; a blend of low density polyethylene and ethylene vinyl acetate, and medium density polyethylene; high density polyethylene, and ethylene vinyl acetate; medium density polyethylene, polypropylene, and high density polyethylene; low density polyethylene, and polyvinyl chloride; an ionomeric polymer, and nylon. The film may comprise three layers either each of a different thermoplastics, or the outer layers being of the same thermoplastics. In the Fig. 4 embodiment, different thermoplastics respectively supplied to the inlets 46, 54 of the adapter are delivered to the rectangular outlet passage 48 thereof on either side of a plate 62 extending across and parallel to the passage walls. In the Fig. 9 embodiment, a pair of the plates 124, 126 extend across the rectangular passage 128, with one thermoplastics being delivered between the plates, and two further different thermoplastics being delivered each from the exterior of-one of the plates. In the Figs. 11 and 12 embodiment (not shown), a pair of the plates (150, 152) is also provided, with one thermoplastics being delivered from between the plates and another thermoplastics being delivered from the exterior of both plates. The relative thickness of each layer of the extruded laminate may be varied by adjustment of the plate, by the speed of the extruders supplying the thermoplastics, or by valving means.
机译:1370355挤出层状塑料LEESONA CORP 1971年9月8日[1970年9月9日]标题B5A将来自不同加热螺杆挤出源的至少两种不同的热塑性塑料组合在平行于矩形侧面的I,B层(图5)中,例如模适配器的方形通道,层从层适配器输送到平面膜模的出口,以作为层压板进行挤出,其中,图6中的每一层在整个挤出宽度上的厚度基本均匀当层在圆形通道中结合时,与在边缘处经历的变化相比,图8(未示出)。通过垂直的三辊堆叠将挤出的薄膜从模具中拉出。挤出物的层可以包含低密度或中密度和高密度聚乙烯,例如聚乙烯或聚乙烯。用于收缩膜;低密度聚乙烯和乙烯乙酸乙烯酯以及中密度聚乙烯的混合物;高密度聚乙烯和乙烯乙酸乙烯酯;中密度聚乙烯,聚丙烯和高密度聚乙烯;低密度聚乙烯和聚氯乙烯;离聚物和尼龙。该膜可包括三层,每一层是不同的热塑性塑料,或者外层是相同的热塑性塑料。在图4的实施例中,分别供应到适配器的入口46、54的不同的热塑性塑料在板62的两侧延伸并延伸到其矩形出口通道48,该板62横跨并平行于通道壁延伸。在图9的实施例中,一对板124、126横跨矩形通道128延伸,其中一种热塑性塑料在板之间被输送,并且另外两种不同的热塑性塑料分别从板之一的外部被输送。在无花果中。在图11和12的实施例(未示出)中,还提供了一对板(150、152),一种热塑性塑料从板之间被输送,另一种热塑性塑料从两个板的外部被输送。挤出层压材料的每一层的相对厚度可通过调节板,通过供应热塑性塑料的挤出机的速度或通过阀装置来改变。

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