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    • 2. 发明授权
    • Polymerization of chloroprene
    • 氯丁二烯的聚合
    • US4786698A
    • 1988-11-22
    • US132975
    • 1987-12-15
    • Rudiger MuschEberhard MullerPeter WendlingWolfgang KonterGerhard Hohmann
    • Rudiger MuschEberhard MullerPeter WendlingWolfgang KonterGerhard Hohmann
    • C08F2/22C08F2/24C08F2/26C08F2/38C08F4/30C08F4/40C08F36/18
    • C08F36/18
    • Gel-free polychloroprene is obtained, at high monomer conversions, using a polymerization initiator comprising sodium dithionite or a mixture of sodium dithionite with formamidinesulphinic acid or with potassium peroxydisulphate or with formamidinesulphinic acid and potassium peroxodisulphate or with potassium peroxodisulphate and sodium anthraquinon-.beta.-sulphonate or with formamidinesulphinic acid and potassium peroxodisulphate and sodium anthraquinone-.beta.-sulphonate, and in the presence of oxygen and a chain transfer agent when 30 to 90% of the initiator is present at the commencement of polymerization and the remainder is added in portions during the polymerization, only further sodium dithionite being added at a conversion >60% in the case of an initiator combination, and when 20 to 80% by weight of the total amount of chain transfer agents is present before or at the commencement of polymerization and the remaining amount is added in one or more parts at monomer conversions of greater than 20%.
    • 使用包含连二亚硫酸钠或连二亚硫酸钠与甲酰胺亚磺酸钠或与过氧二硫酸钾或与甲脒亚磺酸和过氧二硫酸钾或与过氧二硫酸钾和蒽醌-β-磺酸钠的混合物的聚合引发剂,以高单体转化率获得无凝胶的聚氯丁二烯 或与甲酰胺亚磺酸和过二硫酸钾和蒽醌-β-磺酸钠反应,并且在氧和链转移剂存在下,当聚合开始时存在30至90%的引发剂,其余部分在 在引发剂组合的情况下,只有进一步的连二亚硫酸钠以60%的转化率加入,并且当在聚合开始之前或在聚合开始时存在20至80重量%的链转移剂的总量 在单体转化时,一个或多个部分加入量 大于20%。
    • 3. 发明授权
    • Polychloroprene mixtures and the use thereof
    • 聚氯丁二烯混合物及其用途
    • US4485216A
    • 1984-11-27
    • US529389
    • 1983-09-06
    • Rudiger MuschWilhelm GobelWolfgang KonterEberhard Muller
    • Rudiger MuschWilhelm GobelWolfgang KonterEberhard Muller
    • C08L33/00C08L7/00C08L11/00C08L21/00C08L33/04C08L27/22
    • C08L11/00C08L2205/02
    • Solid polychloroprene mixtures consisting of sol and gel polymer, wherein the sol component consists of a copolymer of chloroprene and from 0.75 to 0.32% by weight of sulphur, based on the total quantity of unsaturated compounds of the sol polychloroprene, and the gel component consists of a copolymer of chloroprene, from 0.4 to 1.0% by weight of sulphur, based on the total quantity of unsaturated compounds of the gel polychloroprene and from 7.5.times.10.sup.-3 to 3.0.times.10.sup.-2 mols, based on 100 g of the total quantity of monomer of the gel polychloroprene, of a compound corresponding to the general formula ##STR1## wherein R.sub.1 and R.sub.2 each represents a hydrogen atom or C.sub.1 -C.sub.4 alkyl group, and X represents a C.sub.2 -C.sub.10 alkylene group,are suitable for the production by extrusion and by calandering of rubber articles which may be subjected to high strains.
    • 由溶胶和凝胶聚合物组成的固体聚氯丁二烯混合物,其中溶胶组分由氯丁二烯和0.75至0.32重量%硫的共聚物组成,基于溶胶聚氯丁二烯的不饱和化合物的总量,凝胶组分由 基于凝胶聚氯丁二烯的不饱和化合物的总量和基于100g单体总量的7.5×10 -3至3.0×10 -2摩尔的氯丁二烯共聚物,为0.4至1.0重量%的硫 的凝胶聚氯丁二烯,其通式为:其中R1和R2各自表示氢原子或C1-C4烷基,X代表C2-C10亚烷基,适用于通过挤出和 通过压缩可能经受高应变的橡胶制品。
    • 10. 发明授权
    • Process for the production of high molecular weight polychloroprene and
its use as a starting material for adhesives
    • 用于生产高分子量聚氯丁二烯的方法及其用作粘合剂的起始材料
    • US4405742A
    • 1983-09-20
    • US280018
    • 1981-06-30
    • Rudiger MuschRudiger SchubartWilhelm GobelHeinrich AlbertsGerhard Hohmann
    • Rudiger MuschRudiger SchubartWilhelm GobelHeinrich AlbertsGerhard Hohmann
    • C08F36/18C09J3/12C08F2/24C08F2/38
    • C08F36/18
    • By adding substances corresponding to the following general formula I ##STR1## in which X=O, S or N--R.sub.5 ; R.sub.1 =hydrogen, C.sub.1 -C.sub.19 -alkyl, C.sub.2 -C.sub.19 -alkenyl, phenyl, C.sub.1 -C.sub.4 -alkylene phenyl, C.sub.5 -C.sub.12 -cycloalkyl or C.sub.5 -C.sub.12 -cycloalkenyl; R.sub.2 =hydrogen, C.sub.1 -C.sub.19 -alkyl, C.sub.2 -C.sub.12 -alkenyl, phenyl or C.sub.1 -C.sub.4 -alkylene phenyl; R.sub.3 =hydrogen, C.sub.1 -C.sub.19 -alkyl, C.sub.2 -C.sub.19 -alkenyl, phenyl, C.sub.1 -C.sub.4 -alkylene phenyl, acryl formyl or acetyl; R.sub.4 and R.sub.5 =same or different, C.sub.1 -C.sub.19 -alkyl, C.sub.2 -C.sub.19 -alkenyl, phenyl, C.sub.1 -C.sub.4 -alkylene phenyl, acryl, C.sub.5 -C.sub.12 -cycloalkyl or C.sub.5 -C.sub.12 -cycloalkenyl; R.sub.4 and R.sub.5 may also form a C.sub.4 -C.sub.7 -ring which may optionally contain an oxygen atom in ether form and the radicals R.sub.1 and R.sub.2 may form a C.sub.5 -C.sub.12 -alkylene bridge or a C.sub.5 -C.sub.12 -alkenylene bridge, the radicals R.sub.1 and R.sub.4 may form a C.sub.2 -C.sub.9 -alkylene bridge and the radicals R.sub.1 and R.sub.3 may form a C.sub.3 -C.sub.10 -alkylene bridge; where R.sub.1 and R.sub.2 are attached, the ring formed may be bridged by a C.sub.1 -C.sub.4 -alkylene bridge and the ring systems formed may be substituted by the radical R.sub.6 which represents hydrogen, C.sub.1 -C.sub.5 -alkyl or C.sub.2 -C.sub.5 -alkenyl, in quantities of from 0.05 to 3% by weight, based on 100 parts by weight of monomer, to the aqueous emulsion polymerization of chloroprene at the beginning of the reaction, during or after polymerization, but at the latest before the residual monomers are removed, high-viscosity polychloroprenes characterized by excellent processing behaviour and product properties are obtained.
    • 通过添加对应于下列通式I(I)的物质,其中X = O,S或N-R 5; R1 =氢,C1-C19 - 烷基,C2-C19 - 烯基,苯基,C1-C4-亚烷基苯基,C5-C12-环烷基或C5-C12-环烯基; R2 =氢,C1-C19 - 烷基,C2-C12-烯基,苯基或C1-C4-亚烷基苯基; R3 =氢,C1-C19 - 烷基,C2-C19 - 烯基,苯基,C1-C4-亚烷基苯基,丙烯酰甲酰基或乙酰基; R 4和R 5相同或不同,C 1 -C 19 - 烷基,C 2 -C 19 - 烯基,苯基,C 1 -C 4亚烷基苯基,丙烯酰基,C 5 -C 12 - 环烷基或C 5 -C 12 - 环烯基; R4和R5还可以形成可以任选地含有醚形式的氧原子的C 4 -C 7环,并且基团R 1和R 2可以形成C 5 -C 12亚烷基桥或C 5 -C 12 - 亚烯基桥,基团R 1和 R4可以形成C 2 -C 9 - 亚烷基桥,基团R 1和R 3可以形成C 3 -C 10亚烷基桥; 其中R 1和R 2连接,所形成的环可以被C 1 -C 4 - 亚烷基桥桥连,所形成的环体系可以被代表氢,C 1 -C 5 - 烷基或C 2 -C 5 - 烯基的基团R 6代替, 在反应开始时,在聚合过程中或之后的氯丁二烯的水乳液聚合中,基于100重量份的单体,以0.05重量%的量计,残留单体除去之前的量高 获得以优异的加工性能和产品性能为特征的粘性聚氯乙烯。