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    • 2. 发明授权
    • Process for the production of polycarbonate
    • 聚碳酸酯生产工艺
    • US5258484A
    • 1993-11-02
    • US902356
    • 1992-06-19
    • Reinhard SchomackerUwe HucksGunther WeymansWolfgang HerrigJurgen Kirsch
    • Reinhard SchomackerUwe HucksGunther WeymansWolfgang HerrigJurgen Kirsch
    • C08G64/22C08G64/24
    • C08G64/24
    • A process for the continuous production of a thermoplastic aromatic polycarbonate is disclosed. Accordingly, in a reactor system which includes a tube reactor and a tank equipped with a stirrer, there are reacted a preheated dialkali diphenolate aqueous solution with gaseous phosgene in CH.sub.2 Cl.sub.2 and/or in chlorobenzene solution containing excess phosgene, in a mixer to form a mixed emulsion. The emulsion is then transported at least partly against the force of gravity into the tube reactor to facilitate a polycondensation reaction and in which after a residence time of at least 10 seconds and without dissipation of the heat of reaction there is added a chain terminator. The heat of reaction is dissipated in said tank and aqueous sodium hydroxide and catalyst are added to complete the reaction. The process according to the invention leads to high yields of phosgene.
    • 公开了连续生产热塑性芳族聚碳酸酯的方法。 因此,在包括管式反应器和装有搅拌器的罐的反应器系统中,在混合器中使预热的二元醇二酚盐水溶液与气态光气在CH 2 Cl 2中和/或含有过量光气的氯苯溶液中反应,形成混合 乳液。 然后将乳液至少部分地抵抗重力输送到管式反应器中以促进缩聚反应,并且其中在至少10秒的停留时间之后并且不消耗反应热量时,添加了链终止剂。 在所述槽中消散反应热,加入氢氧化钠水溶液和催化剂以完成反应。 根据本发明的方法导致高产率的光气。
    • 7. 发明授权
    • Process for isolating polycarbonates with CO.sub.2 under pressure
    • 在压力下用二氧化碳分离聚碳酸酯的方法
    • US5221731A
    • 1993-06-22
    • US888942
    • 1992-05-26
    • Gunther WeymansJurgen KirschWolfgang HerrigHanns-Ingolf PaulRolf Treckmann
    • Gunther WeymansJurgen KirschWolfgang HerrigHanns-Ingolf PaulRolf Treckmann
    • C08G64/40C08J3/14
    • C08G64/403
    • A continuous process for the isolation of polycarbonates from a solution of polycarbonate in methylene chloride at temperatures of 30.degree. to 80.degree. C. is disclosed. The process which yields polycarbonate in powder form having residual solvent content of less than 5% by weight, is characterized in that it entails the following steps:a) obtaining a solution of polycarbonate in methylene chloride containing 10 to 40 percent polycarbonate, said percent being relative to the total weight of the polycarbonate solution,b) mixing into said solution under pressures of 10 to 50 bar and at temperatures of 30.degree. to 50.degree. C. a fluid containing carbon dioxide resulting in a non-gelling polycarbonate/methylene/chloride/dioxide pressurized system, in which between 10 and 12% CO.sub.2 are dissolved,c) mixing said pressurized system in a two-component nozzle with additional fluid containing carbon dioxide under a pressure of 50 to 300 bar and at temperatures of 40.degree. to 150.degree. C., to cause rapid precipitation of polycarbonate in the form of solid particles, the quantitative ratio of CO.sub.2 to solution being between 1.0 and 15, preferably between 2.5 and 8.0,f) separating methylene chloride and carbon dioxide gases in a compressor/condenser system.The process is further characterized in that a time interval of at least 0.1 second separates step b) and step c), and in that the input of the fluid containing carbon dioxide is controlled to prevent gelatin in step b) and in that the pressurized system is above the gelation range in step c).
    • 公开了一种在聚碳酸酯从二氯甲烷溶液中分离聚碳酸酯的连续方法,其温度为30℃至80℃。 产生具有小于5重量%的残留溶剂含量的粉末形式的聚碳酸酯的方法的特征在于其需要以下步骤:a)获得聚碳酸酯在含有10-40%聚碳酸酯的二氯甲烷中的溶液,所述百分比为 相对于聚碳酸酯溶液的总重量,b)在10至50巴的压力和30至50℃的温度下将所述溶液混合到含有二氧化碳的流体中,得到非胶凝聚碳酸酯/亚甲基/氯化物 二氧化碳加压系统,其中溶解有10至12%的二氧化碳,c)将所述加压系统混合在双组分喷嘴中,在50至300巴的压力和40至150℃的温度下将含有二氧化碳的另外的流体混合 为了引起固体颗粒形式的聚碳酸酯的快速沉淀,CO 2与溶液的定量比在1.0和15之间,优选在2.5和8.0之间,f)sepa 在压缩机/冷凝器系统中评估二氯甲烷和二氧化碳气体。 该方法的特征还在于,至少0.1秒的时间间隔分离步骤b)和步骤c),并且控制含二氧化碳的流体的输入以防止步骤b)中的明胶,并且加压系统 在步骤c)中的凝胶化范围之上。