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A process for the preparation of a stretched products made from polyethylene of a very high molecular weight.

机译:一种由非常高分子量的聚乙烯制成的拉伸产品的制备方法。

摘要

A stretched article of ultrahigh-molecular-weight polyethylene is produced by (1) melt-kneading a mixture composed of (A) 15 to 80 parts by weight, per 100 parts by weight of components (A) and (B), of ultrahigh-molecular-weight polyethylene having an inherent viscosity [ eta ], determined at 135 DEG C in decalin, of at least 5 dl/g, and (B) 85 to 20 parts by weight, per 100 parts by weight of components (A) and (B), of an aliphatic compound (b1) of at least 8 carbon atoms having a melting point, determined by the DSC method, of at least 10 DEG C and a boiling point of at least 130 DEG C and selected from aliphatic carboxylic acids, aliphatic alcohols, aliphatic acid amides, aliphatic carboxylic acid esters, aliphatic mercaptans, aliphatic aldehydes and aliphatic ketones, optionally up to 80% by weight of the aliphatic compound (b1) being replaced by a hydrocarbon polymer (b2) having a softening point, determined by the method of JIS K-2531,of not more than 130 DEG C and a weight average molecular weight (Mw), determined by the GPC method, of not more than 2,000, in a screw extruder while maintaining the mixture at a temperature from the melting point, determined by the DSC method, of the mixture to 300 DEG C, (2) melt-extruding the molten mixture through a die kept at a temperature from the melting point, determined by the DSC method, of the mixture to 300 DEG C, (3) cooling the resulting unstretched extrudate to solidify it, and (4) subjecting the unstretched solidified extrudate to a stretching treatment at a temperature from the melting point, determined by the DSC method, of component (B) to a point 20 DEG C above the melting point of the mixture at a stretch ratio of either at least 3:1 when step (2) is carried out while a draft is applied to the unstretched extrudate or at least 10:1 when step (2) is carried out in the absence of a draft.
机译:超高分子量聚乙烯的拉伸制品是通过以下方式制备的:(1)将每100重量份组分(A)和(B)的(A)15至80重量份的超高含量的混合物熔融捏合分子量聚乙烯,在135℃萘烷中测定的特性粘度[η]为至少5 dl / g,(B)85至20重量份,基于100重量份的组分(A) (B)至少8个碳原子的脂肪族化合物(b1),其通过DSC方法测定的熔点至少为10℃,沸点至少为130℃,并且选自脂肪族羧酸。酸,脂族醇,脂族酰胺,脂族羧酸酯,脂族硫醇,脂族醛和脂族酮,视情况可多达80%的脂族化合物(b1)被具有软化点的烃聚合物(b2)取代根据JIS K-2531的方法测定,不超过130℃,平均重量在螺杆挤出机中,通过GPC法测定的Ge分子量(Mw)不大于2,000,同时将混合物保持在由DSC方法测定的熔点至300℃的温度下,( 2)通过模具将熔融混合物熔融挤出,该模具的温度保持在通过DSC方法测定的熔点至300℃,(3)冷却所得的未拉伸挤出物使其固化,和(4)使未拉伸的固化挤出物在从DSC法测定的熔点(B)的熔点至混合物的熔点以上20℃的温度下以至少3的拉伸比进行拉伸处理。当在未拉伸的挤出物上施加牵伸力的情况下执行步骤(2)时为1:1,或者在没有牵伸力的情况下执行步骤(2)时为至少10:1。

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