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    • 23. 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%。
    • 24. 发明授权
    • Process for the production of polymers having reactive end groups
    • 用于生产具有反应性端基的聚合物的方法
    • US4611037A
    • 1986-09-09
    • US762948
    • 1985-08-06
    • Rudiger MuschOskar NuykenStephen D. PaskAxel VischerMichael Walter
    • Rudiger MuschOskar NuykenStephen D. PaskAxel VischerMichael Walter
    • C08F4/00C08F2/04C08F2/06C08F2/38C08F4/06C08F8/24C08F10/00C08F16/00C08F16/12
    • C08F110/10
    • An improved process for the production of polymers having halogen end groups from cationically polymerizable monomers, the monomer being polymerized in an inert solvent at a temperature of from +10.degree. to -130.degree. C. using a catalyst system consisting of a metal halide and an organic halide, compounds corresponding to the following general formula being used as organic halides: ##STR1## wherein X represents a halogen atom;R.sub.1, R.sub.2, R.sub.3, represent C.sub.5 -C.sub.10 cycloalkyl, or a C.sub.1 -C.sub.20 straight- or branched-chain alkyl or ##STR2## wherein R.sub.4 and R.sub.5 represent C.sub.5 -C.sub.10 -cycloalkyl or a C.sub.1 -C.sub.20 straight- or branched-chain alkyl;and the organic halide has at least 5 carbon atoms and at most 50 carbon atoms and is in a concentration of from 10.sup.-1 to 10.sup.-6 mols per mol of monomer, while BX.sub.3, SnX.sub.4, TiX.sub.4, SbX.sub.5 or FeX.sub.3, wherein X is fluorine, chlorine, bromine or iodine, is used as metal halide in from 2 to 500 times molar excess, based on the organic halide.
    • 一种用于生产具有来自阳离子可聚合单体的卤素端基的聚合物的改进方法,所述单体在惰性溶剂中在+ 10℃至-130℃的温度下聚合,使用由金属卤化物和 有机卤化物,对应于以下通式的化合物用作有机卤化物:其中X表示卤素原子; R1,R2,R3代表C5-C10环烷基或C1-C20直链或支链烷基或者其中R4和R5代表C5-C10-环烷基或C1-C20直链或支链烷基 ; 并且有机卤化物具有至少5个碳原子和至多50个碳原子,并且每摩尔单体的浓度为10-1至10-6摩尔,而BX3,SnX4,TiX4,SbX5或FeX3,其中X为 氟,氯,溴或碘作为金属卤化物,以有机卤化物计,其摩尔过量为2至500倍。
    • 26. 发明授权
    • Xanthogen disulphides
    • 黄原酸二硫化物
    • US4528388A
    • 1985-07-09
    • US323993
    • 1981-11-23
    • Gunter ArendHeinrich KonigshofenPeter MullerRudiger Musch
    • Gunter ArendHeinrich KonigshofenPeter MullerRudiger Musch
    • C07C67/00C07C325/00C07C329/14C07C329/16C07D317/24C07D319/06C08F2/00C08F2/38C08F36/00C08F36/18C08F136/18C09J121/00C07D317/12
    • C08F36/18C07C329/00C07D319/06
    • Xanthogen disulphides of the following formula: ##STR1## wherein R and R.sub.1 independently represent hydrogen, C.sub.1 -C.sub.6 alkyl, C.sub.5 -C.sub.8 -cycloalkyl or an oxygen-containing heterocyclic ring system having from 5 to 8 ring members and optionally mono- or tri-substituted by C.sub.1 -C.sub.4 -alkyl, and whereinR and R.sub.1 may also be connected together to complete a hetero cyclic ring having from 3 to 6 carbon atoms and from 1 to 3 oxygen ring members, and the ring may be substituted by from 1 to 3 C.sub.1 -C.sub.4 -alkyl groups, with a content of elemental sulphur of less than 1.7% by weight, a process for their production by the reaction of a xanthic acid-O-ester-alkali metal salt of the following formula: ##STR2## wherein R and R.sub.1 are as defined in claims 1 and 3, andM represents an alkali metal, with aqueous chlorine bleach liquor, characterized in that aqueous chlorine bleach liquor having a concentration of less than 0.9 mol NaOCl/kg is used, and oxidation is carried out at a temperature of from 10.degree. to 20.degree. C. and at a pH of from 8 to 12, only until from 0.1 to 5.0 mol % of the xanthic acid-O-ester-alkali metal salt, based on the quantity used, is still present at the end of the reaction, as well as their use as molecular weight regulators in the polymerization of chloroprene.
    • 下式的Xanthogen二硫化物:其中R和R 1独立地表示氢,C 1 -C 6烷基,C 5 -C 8环烷基或含有5至8个环成员的含氧杂环体系,以及任选的单 - 或三 - 被C 1 -C 4烷基取代,并且其中R和R 1也可以连接在一起以完成具有3至6个碳原子和1至3个氧环成员的杂环,并且所述环可以被1至 3个C 1 -C 4烷基,其元素硫含量小于1.7重量%,其通过下式的黄原酸-O-酯 - 碱金属盐反应生产的方法: 其中R和R 1如权利要求1和3中所定义,M表示碱金属,含氯漂白液,其特征在于使用浓度小于0.9mol NaOCl / kg的氯水漂白液,氧化为 在10〜20℃的温度下进行 在8至12的pH下,基于所用的量,在反应结束时,仍然存在黄原酸-O-酯 - 碱金属盐直到0.1至5.0摩尔%,以及它们 在氯丁二烯的聚合中用作分子量调节剂。
    • 28. 发明授权
    • Process for the production of vulcanizable mercaptan-and/or xanthogen
disulfide-regulated polychloroprene rubbers with minimal mold fouling
    • 生产可硫化硫醇和/或黄原二硫键调节聚氯丁二烯橡胶的方法,具有最小的模具污染
    • US5298580A
    • 1994-03-29
    • US946655
    • 1992-09-18
    • Peter WendlingWerner ObrechtMichael HappRudiger MuschEberhard Muller
    • Peter WendlingWerner ObrechtMichael HappRudiger MuschEberhard Muller
    • C08F2/22C08F2/24C08F2/26C08F2/38C08F2/44C08F36/18
    • C08F36/18
    • Vulcanizable, mercaptan- and/or xanthogen-disulfide-regulated polychloroprene rubber are produced by emulsion polymerization of chloroprene and, based on polymerizable monomer used, 0 to 30 parts by weight ethylenically unsaturated, other monomers copolymerizable with chloroprene in an alkaline medium by a process in which(1) 0.1 to 10 parts by weight of a tricyclic diterpene carboxylic acid containing at least two conjugated C.dbd.C double bonds per molecule, based on the polymerizable monomer used, and optionally(2) 0.1 to 5 parts by weight, based on polymerizable monomer used, fatty acid estersare used for their production.The polychloroprene produced in accordance with the invention may be used for the production of vulcanized rubber articles. The polychloroprene rubbers produced by the process according to the invention have a minimal tendency to foul metal molds. The pollution of wastewaters by the process according to the invention is minimal. The well-known favorable properties of polychloroprene remain unaffected.
    • 通过氯丁二烯的乳液聚合制备可硫化,硫醇和/或黄原二硫化物调节的聚氯丁二烯橡胶,并且基于所使用的可聚合单体,0至30重量份烯键式不饱和,可通过工艺在碱性介质中与氯丁二烯共聚的其它单体 其中(1)基于所使用的可聚合单体,每分子含有至少两个共轭C = C双键的三环二萜羧酸0.1至10重量份,和任选地(2)0.1至5重量份的基于 在使用的可聚合单体上,使用脂肪酸酯来制造。 根据本发明生产的聚氯丁二烯可用于硫化橡胶制品的生产。 通过根据本发明的方法生产的聚氯丁二烯橡胶具有污染金属模具的最小趋势。 通过根据本发明的方法对废水的污染是最小的。 聚氯丁二烯的众所周知的有利特性保持不变。