Blends of polyolefins with polymers containing reactive agents
    1.
    发明授权
    Blends of polyolefins with polymers containing reactive agents 失效
    聚烯烃与含有反应剂的聚合物的共混物

    公开(公告)号:US4678834A

    公开(公告)日:1987-07-07

    申请号:US756223

    申请日:1985-07-18

    CPC分类号: C08J3/226 C08J2323/02

    摘要: A polyolefin blend comprising, in physical admixture, a major portion of particles of a polyethylene and a minor portion of particles of a composition of a thermoplastic second polymer, is disclosed. The polyethylene is selected from the group consisting of homopolymers of ethylene and copolymers of ethylene and at least one C.sub.4 -C.sub.10 higher alpha-olefin, and the second polymer is a normally solid thermoplastic polymer having a melting point of less than 185.degree. C. and a shear viscosity that is not more than that of the polyethylene when measured at 200.degree. C. and a shear rate of 400 sec.sup.-1 with the proviso that the second polymer is not a homopolymer or copolymer derived solely from hydrocarbon alpha-olefins having 2-10 carbon atoms. Examples of second polymers are (a) homopolymers and copolymers of unsaturated hydrocarbons in which at least one monomer is other than a C.sub.2 -C.sub.10 alpha-olefin, e.g. ethylene/propylene elastomers, polystyrene and styrene/butadiene/styrene copolymers, (b) copolymers of ethylene with ethylenically unsaturated carboxylic acids and anhydrides, and esters thereof, and (c) modified polymers e.g. chlorinated polyethylene, grafted and ionomeric polymers. The composition of the second polymer contains a reactive agent that is capable of reacting with polyolefins that are in a molten state, such agents being cross-linking agents and/or modifying agents. In an alternative embodiment, the polyethylene may be more broadly defined as being a homopolymer or copolymer of hydrocarbon alpha-olefins having 2-10 carbon atoms. The blends may be used in a wide variety of processes, including blow-moulding processes, film and pipe extrusion processes, sheet thermoforming processes and rotational moulding processes.

    摘要翻译: 公开了一种聚烯烃共混物,其以物理混合物形式包含主要部分的聚乙烯颗粒和少部分热塑性第二聚合物组合物颗粒的颗粒。 聚乙烯选自乙烯均聚物和乙烯与至少一种C 4 -C 10高级α-烯烃的共聚物,第二聚合物是熔点小于185℃的通常为固体的热塑性聚合物, 在200℃下测量的剪切粘度不大于聚乙烯的剪切粘度,剪切速率为400秒-1,条件是第二聚合物不是仅由具有2个碳原子的α-烯烃的均聚物或共聚物 -10个碳原子。 第二聚合物的实例是(a)不饱和烃的均聚物和共聚物,其中至少一种单体不是C 2 -C 10α-烯烃,例如, 乙烯/丙烯弹性体,聚苯乙烯和苯乙烯/丁二烯/苯乙烯共聚物,(b)乙烯与烯属不饱和羧酸和酸酐的共聚物及其酯,和(c) 氯化聚乙烯,接枝和离聚物聚合物。 第二聚合物的组成包含能够与处于熔融状态的聚烯烃反应的反应剂,这些试剂是交联剂和/或改性剂。 在替代实施方案中,聚乙烯可以更广泛地定义为具有2-10个碳原子的烃α-烯烃的均聚物或共聚物。 共混物可以用于各种各样的方法,包括吹塑工艺,薄膜和管材挤出方法,片材热成型方法和旋转模塑方法。

    Reduction of isomerization in solution process for polymerization of
alpha-olefins
    2.
    发明授权
    Reduction of isomerization in solution process for polymerization of alpha-olefins 失效
    在α-烯烃聚合反应的溶液中减少异构化

    公开(公告)号:US4777229A

    公开(公告)日:1988-10-11

    申请号:US95689

    申请日:1987-09-14

    CPC分类号: C08F2/06 C08F10/00 C08F210/16

    摘要: A solution polymerization process for the preparation of high molecular weight polymers selected from the group consisting of homopolymers of ethylene and copolymers of ethylene and butene-1 is disclosed. The process comprises feeding monomer(s), coordination catalyst and inert hydrocarbon solvent to a reactor, polymerizing the monomers at a temperature of up to 320.degree. C. and a pressure of less than 25 MPa, and deactivating the catalyst in the solution so obtained. The catalyst is deactivated by sequentially admixing therewith a minor amount of dimethyl carbonate followed by a solution of a salt of an alkaline earth metal or zinc and an aliphatic monocarboxylic acid dissolved in hydrocarbon solvent. The hydrocarbon solvent and other volatile matter are then separated from the resultant solution and a composition comprising the high molecular weight polymer is recovered. The amount of dimethyl carbonate is not more than 2.5 moles, per mole of halogen plus alkyl radicals in the coordination catalyst.

    摘要翻译: 公开了用于制备选自乙烯均聚物和乙烯和丁烯-1的共聚物的高分子量聚合物的溶液聚合方法。 该方法包括将单体,配位催化剂和惰性烃溶剂进料到反应器中,在高达320℃的温度和小于25MPa的压力下使单体聚合,并使所得溶液中的催化剂失活 。 通过依次与少量的碳酸二甲酯混合,然后将碱土金属或锌的盐和溶解在烃溶剂中的脂肪族单羧酸的溶液依次混合,使催化剂失活。 然后将烃溶剂和其它挥发性物质与所得溶液分离,并回收包含高分子量聚合物的组合物。 在配位催化剂中,每摩尔卤素加上烷基,碳酸二甲酯的量不超过2.5摩尔。

    Process for the grafting of monomers onto polyolefins
    3.
    发明授权
    Process for the grafting of monomers onto polyolefins 失效
    将单体接枝到聚烯烃上的方法

    公开(公告)号:US4612155A

    公开(公告)日:1986-09-16

    申请号:US756176

    申请日:1985-07-18

    CPC分类号: C08F255/02

    摘要: A continuous process for the grafting of ethylenically unsaturated monomers onto homopolymers of ethylene and copolymers of ethylene and C.sub.4 -C.sub.10 higher alpha-olefins is disclosed. The process involves feeding to an extruder an admixture comprising (i) a major portion of the above polymer of ethylene, (ii) the monomer, (iii) 25-500 ppm of an organic peroxide and (iv) a minor portion of a normally solid thermoplastic polymer having a melting point of less than 185.degree. C. and a shear viscosity at 200.degree. C. and a shear rate of 400 sec.sup.-1 that is not more than 50% of that of the polymer of ethylene. The organic peroxide is in the form of a composition with the thermoplastic polymer. The admixture is mixed in a first zone at a temperature above the melting point of the polymers for at least ten seconds but for less than 25% decomposition of the peroxide and then in a second zone for a period that is at least four times the half-life of the peroxide. A grafted polymer having a melt index that is 20-100% of that of the polymer prior to grafting is obtained. The grafted polymer may be used in a variety of end-uses, for example, the manufacture of film, moulding of articles, extrusion coating of metals and coextrusion processes.

    摘要翻译: 公开了将乙烯不饱和单体接枝到乙烯均聚物和乙烯与C 4 -C 10高级α-烯烃共聚物上的连续方法。 该方法包括向挤出机中加入混合物,该混合物包含(i)上述乙烯聚合物的主要部分,(ii)单体,(iii)25-500ppm有机过氧化物和(iv)少量正常的 熔点小于185℃的固体热塑性聚合物和200℃下的剪切粘度和400秒-1的剪切速率,其不超过乙烯聚合物的50%。 有机过氧化物是具有热塑性聚合物的组合物的形式。 将混合物在高于聚合物熔点的温度的第一区域中混合至少十秒,但是少于25%的过氧化物分解,然后在第二区域中至少是四分之一的时间 过氧化物的生命。 得到在接枝前熔体指数为聚合物的20-100%的接枝聚合物。 接枝聚合物可以用于各种最终用途,例如膜的制造,制品的成型,金属的挤出涂覆和共挤出方法。

    Catalytic oxidation of cycloparaffins
    4.
    发明授权
    Catalytic oxidation of cycloparaffins 失效
    环烷烃的催化氧化

    公开(公告)号:US4341907A

    公开(公告)日:1982-07-27

    申请号:US229873

    申请日:1981-01-30

    申请人: Ronald A. Zelonka

    发明人: Ronald A. Zelonka

    摘要: A process is disclosed for the catalytic oxidation of a cycloparaffin, e.g., cyclohexane, to partial oxidation products thereof, especially for the production of mixtures of cycloalkanols and cycloalkanones. In the process, molecular oxygen, usually in the presence of an inert gas, is introduced into the cycloparaffin at elevated pressure and a temperature of 130.degree.-180.degree. C., in the presence of an oxidation catalyst comprising a heavy metal compound along with an N-heterocyclic compound. The heavy metal of the heavy metal compound may be cobalt, vanadium, manganese, copper, iron or nickel. The heavy metal compound may have ligands of alkanoate, dialkylphosphate, dicycloalkylphosphate or alkylcycloalkylphosphate. The N-heterocyclic compound may be dipyridyl, pyrimidine, pyrazine, pyridine and pyridine substituted with --CN, --R, and/or --OR where R is alkyl. A preferred catalyst is cobalt bis[di(2-ethylhexyl)phosphate] in combination with pyridine.

    摘要翻译: 公开了一种用于将环烷烃(例如环己烷)催化氧化成其部分氧化产物,特别是用于生产环烷醇和环烷酮的混合物的方法。 在此过程中,通常在惰性气体存在下,分子氧在升高的压力和130〜-180℃的温度下,在包含重金属化合物的氧化催化剂存在下引入环烷烃 N-杂环化合物。 重金属化合物的重金属可以是钴,钒,锰,铜,铁或镍。 重金属化合物可以具有链烷酸酯,磷酸二烷基酯,磷酸二环烷基酯或磷酸烷基环烷基酯的配体。 N-杂环化合物可以是吡啶基,嘧啶,吡嗪,吡啶和被-CN,-R和/或-OR取代的吡啶,其中R是烷基。 优选的催化剂是双[二(2-乙基己基)磷酸酯]钴与吡啶的组合。