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    • 3. 发明授权
    • Method for isolating polymers from solutions
    • 从溶液中分离聚合物的方法
    • US06506281B1
    • 2003-01-14
    • US09719891
    • 2001-03-02
    • Clemens CasperJörgen WeinschenckKlemens KohlgrüberJürgen HeuserChristian KordsThomas Elsner
    • Clemens CasperJörgen WeinschenckKlemens KohlgrüberJürgen HeuserChristian KordsThomas Elsner
    • B01D122
    • B01D3/06C08G64/406Y10S159/08Y10S159/10
    • A process of evaporating a viscous polymer solution is described. The process includes: (a) providing a viscous polymer solution including at least 30 wt. % of solvents and monomers; (b) introducing the viscous polymer solution into a heated helix (5), the heated helix having a vapor exit velocity of 200 to 300 m/s, (a film flow including a two-phase mixture of polymer melt, and solvent vapors and monomer vapors being formed within the helix); (c) forwarding the film flow from helix (5) into a heated vapor separator (6); (d) expanding the two-phase mixture of polymer melt, and solvent vapors and monomer vapors of the film flow within vapor separator (6) at an absolute pressure of 10 mbar to 800 mbar, (a bottom product including a concentrated melt of the polymer is formed within the vapor separator); and (e) withdrawing the bottom product from vapor separator (6). Each of the helix (5) and vapor separator (6) have a separate heating device, and each of heating device independently provides a temperature that is above the softening point of the polymer.
    • 描述蒸发粘性聚合物溶液的方法。 该方法包括:(a)提供粘性聚合物溶液,其包含至少30wt。 %的溶剂和单体; (b)将粘性聚合物溶液引入加热的螺旋(5)中,加热的螺旋具有200-300m / s的蒸气出口速度(包括聚合物熔体和溶剂蒸气的两相混合物的膜流和 单体蒸气在螺旋内形成); (c)将膜流从螺旋(5)转移到加热的蒸气分离器(6)中; (d)在10毫巴至800毫巴的绝对压力下,将蒸气分离器(6)内的聚合物熔体和溶剂蒸气和单体蒸气的溶剂蒸气和单体蒸气膨胀(包括含有 聚合物形成在蒸气分离器内); 和(e)从蒸气分离器(6)中取出底部产物。 螺旋(5)和蒸汽分离器(6)中的每一个具有单独的加热装置,并且每个加热装置独立地提供高于聚合物软化点的温度。
    • 4. 发明授权
    • Method and device for evaporating polymer solutions of thermoplastic polymers, and a polycarbonate which can be obtained by evaporation
    • 用于蒸发热塑性聚合物的聚合物溶液的方法和装置,以及可以通过蒸发获得的聚碳酸酯
    • US06545122B1
    • 2003-04-08
    • US10019352
    • 2001-10-19
    • Thomas ElsnerJürgen HeuserChristian Kords
    • Thomas ElsnerJürgen HeuserChristian Kords
    • C08J300
    • C08G64/403B01D3/06B01D19/0005
    • Described is a multi-stage, continuous process for evaporating and concentrating feed polymer solutions. In a first stage (a) of the process, the feed polymer solution is concentrated by passing it through one of (i) a combination of a tubular heat exchanger with one of a thin-film evaporator and a coiled tube evaporator, and (ii) a tubular heat exchanger. Each evaporator of (i) having a downstream separator. In a further stage (b), the intermediate polymer solution of the first stage is further concentrated and degassed to form a product polymer in a tubular heat exchanger having a downstream separator. The tubular heat exchanger of the further stage has an inside diameter of from 5 to 30 mm, and a length of from 0.5 to 4 m, and the throughput per heat exchanger tube being from 5 to 30 kg/h, based on the polymer. An entrainer is introduced into a delivery device located downstream from the separator of further stage (b). The product concentrated/degassed polymer of further stage (b) is then isolated and optionally granulated. Also described is an apparatus for evaporating and concentrating feed polymer solutions.
    • 描述了用于蒸发和浓缩饲料聚合物溶液的多阶段连续方法。 在该方法的第一阶段(a)中,通过使进料聚合物溶液通过(i)管式热交换器与薄膜蒸发器和盘管式蒸发器之一的组合, )管式热交换器。 (i)的每个蒸发器具有下游分离器。 在另一阶段(b)中,将第一阶段的中间聚合物溶液进一步浓缩并脱气以在具有下游分离器的管式热交换器中形成产物聚合物。 基于聚合物,进一步的管状热交换器的内径为5至30mm,长度为0.5至4m,每个热交换器管的产量为5至30kg / h。 将夹带剂引入位于进一步的阶段(b)的分离器下游的递送装置中。 然后分离另外阶段(b)的产物浓缩/脱气聚合物并任选地造粒。 还描述了用于蒸发和浓缩进料聚合物溶液的装置。
    • 9. 发明授权
    • Device and method for degassing plastics
    • 塑料脱气装置及方法
    • US06811294B1
    • 2004-11-02
    • US09937467
    • 2001-09-25
    • Thomas ElsnerJürgen HeuserChristian Kords
    • Thomas ElsnerJürgen HeuserChristian Kords
    • B29B748
    • B29C47/767B29C47/0009B29C47/762B29C47/825C08G64/406
    • An apparatus for degassing plastic materials, e.g., high molecular weight polycarbonate solutions, is described. The apparatus includes a double-shaft extruder having a length-to-diameter ratio of less than or equal to 40, which comprises: (i) two co-rotating and meshing shafts; (ii) an intake opening; and (iii) upstream and downstream portions relative to the intake opening. The shafts of the extruder are designed with a double lead in a degassing zone, and with a triple lead in a pressure build-up zone. Each of the degassing and the pressure build-up zones are down-stream from the intake opening, and the pressure build-up zone is further down-stream than the degassing zone. Also described is a process for degassing plastic materials, which involves providing the described double-shaft co-rotating extruder, into which plastic material is fed, processed and degassed. Entraining agents, such as nitrogen, and other processing additives may be introduced into an extruder during the process of the present invention.
    • 描述了用于对塑料材料(例如高分子量聚碳酸酯溶液)进行脱气的设备。 该设备包括长径比小于或等于40的双轴挤出机,其包括:(i)两个共同旋转和啮合的轴; (ii)进气口; 和(iii)相对于进气口的上游和下游部分。 挤出机的轴设计为具有脱气区域中的双引线,并且在压力增加区域中具有三重引线。 每个脱气和压力积聚区域从进气口向下游,并且压力积聚区域比脱气区域进一步下游。 还描述了一种用于对塑料材料进行脱气的方法,其涉及提供所描述的双轴同向旋转挤出机,塑料进料,加工和脱气。 在本发明的方法中,可将引入剂如氮气和其它加工添加剂引入挤出机中。