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    • 1. 发明授权
    • Continuous production of reduced gel content hydroxylated addition
polymers
    • 连续生产降低凝胶含量的羟基化加成聚合物
    • US5508366A
    • 1996-04-16
    • US325001
    • 1994-10-18
    • Kevin M. AndristJ. David CampbellRichard W. ChyllaRakesh K. Popli
    • Kevin M. AndristJ. David CampbellRichard W. ChyllaRakesh K. Popli
    • C08F2/06C08F220/18C08F220/28C08F220/30C08F20/26
    • C08F220/28
    • A process is disclosed for the continuous production, with reduced gel formation, of free radical addition polymers from ethylenically unsaturated monomers containing at least one free hydroxyl group such as 2-hydroxyethyl methacrylate, from about 0 to about 5% by weight of an alpha-beta unsaturated carboxylic acid such as acrylic acid or methacrylic acid, and the remainder of the monomers used are free radical addition copolymerizable compounds such as styrene, methyl methacrylate and butyl acrylate. The free radical addition polymerization is conducted at from about 150.degree. C. to about 310.degree. C. under superatmospheric pressure in the presence of one or more solvents. The solvent or the volume average of the solvent mixture has an overall calculated root mean square value of the hydrogen bonding and polar contributions of each solvent's solubility parameters in the range of from about 6 to about 15. The solvent or solvents in total have sufficient volatility under the conditions being used to conduct the polymerization such that any liquid condensate of vapor mixture forming on interior surfaces of the reactor equipment located above the surface of the monomer reactants contains at least 50 mole percent of the solvent to reduce gel formation on such interior surfaces. The process permits the continuous polymerization of the polymers over extended periods of time with reduced formation of gel particles and gel deposits.
    • 公开了一种用于连续生产的方法,其具有减少的凝胶形成,从含有至少一个游离羟基的烯键式不饱和单体(例如甲基丙烯酸2-羟乙酯),约0至约5重量%的α-烯属不饱和单体, β不饱和羧酸如丙烯酸或甲基丙烯酸,其余所用的单体是自由基加成可共聚合的化合物,如苯乙烯,甲基丙烯酸甲酯和丙烯酸丁酯。 在大气压下,在一种或多种溶剂的存在下,自由基加成聚合在约150℃至约310℃下进行。 溶剂混合物的溶剂或体积平均值具有氢键的总计算的均方根值和每种溶剂的溶解度参数的极性贡献在约6至约15的范围内。溶剂或溶剂总共具有足够的挥发性 在用于进行聚合的条件下,使得形成在位于单体反应物表面之上的反应器设备的内表面上的蒸气混合物的任何液体冷凝物含有至少50摩尔%的溶剂以减少在这些内表面上的凝胶形成 。 该方法允许聚合物在延长的时间段内连续聚合,减少了凝胶颗粒和凝胶沉积物的形成。
    • 5. 发明授权
    • Process for producing hyperbranched polymers
    • 制备超支化聚合物的方法
    • US5986020A
    • 1999-11-16
    • US906140
    • 1997-08-05
    • J. David CampbellFouad Teymour
    • J. David CampbellFouad Teymour
    • C08F2/01B01J19/24C08F2/00C08F2/02C08F212/04C08F36/00C08G85/00
    • C08F212/04B01J19/2465C08F2/02B01J2219/0006B01J2219/00094B01J2219/00164
    • A method is provided for producing hyperbranched polymers comprising heating a polymerizable reaction charge comprising (a) a monomer mixture comprising 50-99.1% by weight of at least one monoethylenically unsaturated monomer and 0.1-50% by weight of one or more multiethylenically unsaturated monomers and (b) if at least one ethylenically unsaturated monomer of the monomer mixture is not a thermally initiating monomer, a free radical polymerization initiator, to a temperature in the range from about 250.degree. C. to about 400.degree. C. in a continuous reactor which allows mixing of the reactor contents for a residence time of from about 2 minutes to about 60 minutes, provided that if the total amount of multiethylenically unsaturated monomer is less than 3% by weight of the monomer mixture than at least one of said one or more multiethylenically unsaturated monomers must be tri- or greater ethylenically unsaturated. The hyperbranched polymers prepared by this process are also described.
    • 提供了一种用于生产超支化聚合物的方法,其包括加热可聚合反应进料,其包含(a)包含50-99.1重量%的至少一种单烯属不饱和单体和0.1-50重量%的一种或多种多烯属不饱和单体的单体混合物, (b)如果单体混合物的至少一种烯属不饱和单体不是热引发单体,即自由基聚合引发剂,在连续反应器中在约250℃至约400℃的温度范围内 允许反应器内容物的混合停留时间为约2分钟至约60分钟,条件是如果多烯键式不饱和单体的总量小于单体混合物的总量,而不是所述一种或多种 多烯属不饱和单体必须是三或更多的烯属不饱和单体。 还描述了通过该方法制备的超支化聚合物。
    • 7. 发明授权
    • Hyperbranched polymers
    • 超支化聚合物
    • US06627720B2
    • 2003-09-30
    • US09873634
    • 2001-06-04
    • J. David CampbellFouad Teymour
    • J. David CampbellFouad Teymour
    • C08F21236
    • C08F212/04B01J19/2465B01J2219/0006B01J2219/00094B01J2219/00164C08F2/02
    • A method is provided for producing hyperbranched polymers comprising heating a polymerizable reaction charge comprising (a) a monomer mixture comprising 50-99.1% by weight of at least one monoethylenically unsaturated monomer and 0.1-50% by weight of one or more multiethylenically unsaturated monomers and (b) if at least one ethylenically unsaturated monomer of the monomer mixture is not a thermally initiating monomer, a free radical polymerization initiator, to a temperature in the range from about 250° C. to about 400° C. in a continuous reactor which allows mixing of the reactor contents for a residence time of from about 2 minutes to about 60 minutes, provided that if the total amount of multiethylenically unsaturated monomer is less than 3% by weight of the monomer mixture than at least one of said one or more multiethylenically unsaturated monomers must be tri- or greater ethylenically unsaturated. The hyperbranched polymers prepared by this process are also described.
    • 提供了一种用于生产超支化聚合物的方法,其包括加热可聚合反应进料,其包含(a)包含50-99.1重量%的至少一种单烯属不饱和单体和0.1-50重量%的一种或多种多烯属不饱和单体的单体混合物, (b)如果单体混合物的至少一种烯键式不饱和单体不是热引发单体,即自由基聚合引发剂,在连续反应器中达到约250℃至约400℃的温度 允许反应器内容物的混合停留时间为约2分钟至约60分钟,条件是如果多烯键式不饱和单体的总量小于单体混合物的总量,而不是所述一种或多种 多烯属不饱和单体必须是三或更多的烯属不饱和单体。 还描述了通过该方法制备的超支化聚合物。
    • 8. 发明授权
    • Hyperbranched polymers
    • 超支化聚合物
    • US06265511B1
    • 2001-07-24
    • US09389821
    • 1999-09-03
    • J. David CampbellFouad Teymour
    • J. David CampbellFouad Teymour
    • C08F21234
    • C08F212/04B01J19/2465B01J2219/0006B01J2219/00094B01J2219/00164C08F2/02
    • A method is provided for producing hyperbranched polymers comprising heating a polymerizable reaction charge comprising (a) a monomer mixture comprising 50-99.1% by weight of at least one monoethylenically unsaturated monomer and 0.1-50% by weight of one or more multiethylenically unsaturated monomers and (b) if at least one ethylenically unsaturated monomer of the monomer mixture is not a thermally initiating monomer, a free radical polymerization initiator, to a temperature in the range from about 250° C. to about 400° C. in a continuous reactor which allows mixing of the reactor contents for a residence time of from about 2 minutes to about 60 minutes, provided that if the total amount of multiethylenically unsaturated monomer is less than 3% by weight of the monomer mixture than at least one of said one or more multiethylenically unsaturated monomers must be tri- or greater ethylenically unsaturated. The hyperbranched polymers prepared by this process are also described.
    • 提供了一种用于生产超支化聚合物的方法,其包括加热可聚合反应进料,其包含(a)包含50-99.1重量%的至少一种单烯属不饱和单体和0.1-50重量%的一种或多种多烯属不饱和单体的单体混合物, (b)如果单体混合物的至少一种烯键式不饱和单体不是热引发单体,即自由基聚合引发剂,在连续反应器中达到约250℃至约400℃的温度 允许反应器内容物的混合停留时间为约2分钟至约60分钟,条件是如果多烯键式不饱和单体的总量小于单体混合物的总量,而不是所述一种或多种的至少一种 多烯属不饱和单体必须是三或更多的烯属不饱和单体。 还描述了通过该方法制备的超支化聚合物。
    • 10. 发明授权
    • Process for the preparation of macromers
    • 制备大分子单体的方法
    • US06388026B1
    • 2002-05-14
    • US08906141
    • 1997-08-05
    • J. David CampbellMichihiro KaaiDavid D. SchatzFouad Teymour
    • J. David CampbellMichihiro KaaiDavid D. SchatzFouad Teymour
    • C08F2018
    • C08F2/02C08F120/12
    • A process for preparing low molecular weight homomacromers and comacromers which includes (a) charging a reactor with (i) ethylenically unsaturated monomers selected from the group consisting of acrylic monomers or monoalkenyl aromatic monomers and (ii) if said ethylenically unsaturated monomer is not a thermally initiating monomer, a free radical polymerizable initiator, to form a polymerizable reaction charge. The reaction charge is heated during continuous mixing in the reactor to reaction temperature in the range from about 180° C. to about 500° C. for a residence time greater than 5 minutes to form the low molecular weight homomacromers or comacromers. If the residence time is 60 minutes or less, the reaction temperature is greater than 270° C. and if the reaction charge is a mixture of acrylic monomer and monoalkenyl monomer and the residence time is 60 minutes or less then the reaction temperature is greater than 310° C.
    • 一种制备低分子量同质异构体和共聚物的方法,其包括(a)向(i)选自丙烯酸单体或单链烯基芳族单体的烯键式不饱和单体和(ii)所述烯属不饱和单体不是热的 引发单体,自由基可聚合引发剂,形成可聚合反应的电荷。 将反应装料在反应器中连续混合期间加热至约180℃至约500℃范围内的反应温度,停留时间大于5分钟以形成低分子量同型异构体或可变光体。 如果停留时间为60分钟以下,则反应温度大于270℃,如果反应物为丙烯酸单体和单烯基单体的混合物,停留时间为60分钟以下,则反应温度大于 310℃