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公开(公告)号:EP0515992B1
公开(公告)日:1995-08-09
申请号:EP92108652.6
申请日:1992-05-22
申请人: NIPPON OIL CO. LTD. , NIPPON PETROCHEMICALS COMPANY, LIMITED , POLYMER PROCESSING RESEARCH INSTITUTE LIMITED
发明人: Kobayashi, Seizo , Nomiyama, Kazutosi , Iwanami, Yoshimu , Yoshida, Sumio , Kurihara, Kazuhiko , Yazawa, Hiroshi
CPC分类号: C08J5/04 , B29B15/122 , B29C43/228 , B29C43/48 , B29C55/18 , B29C70/504 , B29C2043/483 , B29K2023/0683 , C08J5/24 , Y10S264/47 , Y10S428/902 , Y10T442/291
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公开(公告)号:EP0515992A1
公开(公告)日:1992-12-02
申请号:EP92108652.6
申请日:1992-05-22
申请人: NIPPON OIL CO. LTD. , NIPPON PETROCHEMICALS COMPANY, LIMITED , POLYMER PROCESSING RESEARCH INSTITUTE LIMITED
发明人: Kobayashi, Seizo , Nomiyama, Kazutosi , Iwanami, Yoshimu , Yoshida, Sumio , Kurihara, Kazuhiko , Yazawa, Hiroshi
CPC分类号: C08J5/04 , B29B15/122 , B29C43/228 , B29C43/48 , B29C55/18 , B29C70/504 , B29C2043/483 , B29K2023/0683 , C08J5/24 , Y10S264/47 , Y10S428/902 , Y10T442/291
摘要: The present invention provides a prepreg obtained by stretching a material comprising, as a main component, an ultra-high-molecular-weight polyethylene having an intrinsic viscosity of 5-50 dl/g as measured at 135 o C in decalin, to a total draw ratio of at least 20, subjecting the resulting stretched polyethylene material to a splitting treatment, and impregnating the resulting material with a thermosetting resin, and a process for producing said prepreg.
The split stretched polyethylene material has improved adhesion to the impregnant resin and can be used as a good base material for prepreg.摘要翻译: 本发明提供一种预浸料,其通过拉伸含有在135℃下在十氢化萘中测定的特性粘度为5-50dl / g的超高分子量聚乙烯作为主要成分的材料, 总拉伸比为至少20,对所得拉伸聚乙烯材料进行裂化处理,并用热固性树脂浸渍所得材料,以及制备所述预浸料的方法。 分散拉伸的聚乙烯材料具有改进的对浸渍树脂的粘附性,并且可以用作预浸料的良好的基材。
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公开(公告)号:EP0237294A2
公开(公告)日:1987-09-16
申请号:EP87301961.6
申请日:1987-03-06
申请人: NIPPON OIL CO. LTD.
发明人: Tajima, Yoshio , Nomiyama, Kazutosi , Nishikitani, Yoshinori , Kuroda, Nobuyuki , Matsuura, Kazuo
CPC分类号: C08F10/02 , C08F10/00 , C08F110/02 , C08F210/16 , Y10S526/905 , C08F2/34 , C08F4/6228 , C08F2500/12 , C08F2500/14 , C08F2500/13 , C08F2500/07 , C08F2500/11 , C08F2500/18 , C08F210/08 , C08F4/6543 , C08F4/69 , C08F4/025
摘要: A process for preparing an ethylene polymer by a two-stage polymerization of ethylene or ethylene and an a-olefin in an inert hydrocarbon at 50-100°C using a coordination polymerization catalyst containing a solid component and an organoaluminum compound, said solid component containing a transition metal compound, which process comprises:
(a) in a first stage, producing 10-90% by weight based on the total polymer quantity of a polymer having a melt index in the range of 0.0001 to 0.5 g/10 min as measured according to ASTM D 1238-73, Condition E, using as said solid component a solid product obtained by supporting chromium trioxide or a compound which on calcining forms chromium oxide at least partially, on an inorganic oxide carrier followed by calcining, and using as said organoaluminum compound a compound of the general formula
wherein R is a hydrocarbon radical having 1 to 18 carbon atoms and n is 2 5 n ≦ 100; and
(b) in a second stage, producing 90-10% by weight based on the total polymer quantity of a polymer having a melt index in the range of 0.01 to 50 g/10 min as measured according to ASTM D 1238-73, Condition E, using as said solid component a solid material containing at least magnesium and titanium, and using as said organoaluminum compound a compound of the general formula AIR'pX 3 - P wherein R' is a hydrocarbon radical having 1 to 20 carbon atoms, X is halogen and/or alkoxy and p is 0
Alternatively the solid component of (a) also contains magnesium and titanium and step (b) is effected simply by adding the compound of the formula AIR'pX 3 -p after completion of the first stage polymerisation.-
公开(公告)号:EP0237294B1
公开(公告)日:1991-12-04
申请号:EP87301961.6
申请日:1987-03-06
申请人: NIPPON OIL CO. LTD.
发明人: Tajima, Yoshio , Nomiyama, Kazutosi , Nishikitani, Yoshinori , Kuroda, Nobuyuki , Matsuura, Kazuo
CPC分类号: C08F10/02 , C08F10/00 , C08F110/02 , C08F210/16 , Y10S526/905 , C08F2/34 , C08F4/6228 , C08F2500/12 , C08F2500/14 , C08F2500/13 , C08F2500/07 , C08F2500/11 , C08F2500/18 , C08F210/08 , C08F4/6543 , C08F4/69 , C08F4/025
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公开(公告)号:EP0237294A3
公开(公告)日:1989-01-25
申请号:EP87301961.6
申请日:1987-03-06
申请人: NIPPON OIL CO. LTD.
发明人: Tajima, Yoshio , Nomiyama, Kazutosi , Nishikitani, Yoshinori , Kuroda, Nobuyuki , Matsuura, Kazuo
CPC分类号: C08F10/02 , C08F10/00 , C08F110/02 , C08F210/16 , Y10S526/905 , C08F2/34 , C08F4/6228 , C08F2500/12 , C08F2500/14 , C08F2500/13 , C08F2500/07 , C08F2500/11 , C08F2500/18 , C08F210/08 , C08F4/6543 , C08F4/69 , C08F4/025
摘要: A process for preparing an ethylene polymer by a two-stage polymerization of ethylene or ethylene and an a-olefin in an inert hydrocarbon at 50-100°C using a coordination polymerization catalyst containing a solid component and an organoaluminum compound, said solid component containing a transition metal compound, which process comprises:
(a) in a first stage, producing 10-90% by weight based on the total polymer quantity of a polymer having a melt index in the range of 0.0001 to 0.5 g/10 min as measured according to ASTM D 1238-73, Condition E, using as said solid component a solid product obtained by supporting chromium trioxide or a compound which on calcining forms chromium oxide at least partially, on an inorganic oxide carrier followed by calcining, and using as said organoaluminum compound a compound of the general formula
wherein R is a hydrocarbon radical having 1 to 18 carbon atoms and n is 2 5 n ≦ 100; and (b) in a second stage, producing 90-10% by weight based on the total polymer quantity of a polymer having a melt index in the range of 0.01 to 50 g/10 min as measured according to ASTM D 1238-73, Condition E, using as said solid component a solid material containing at least magnesium and titanium, and using as said organoaluminum compound a compound of the general formula AIR'pX 3 - P wherein R' is a hydrocarbon radical having 1 to 20 carbon atoms, X is halogen and/or alkoxy and p is 0 Alternatively the solid component of (a) also contains magnesium and titanium and step (b) is effected simply by adding the compound of the formula AIR'pX 3 -p after completion of the first stage polymerisation.
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