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    • 4. 发明申请
    • Fluidized-bed Vaporisation Dryer
    • 流化床蒸发干燥器
    • US20170045293A1
    • 2017-02-16
    • US15307716
    • 2015-03-09
    • BMA BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG
    • Gerald CaspersHartmut HafemannCarsten BonathHolger Fersterra
    • F26B17/10F26B25/00
    • F26B17/107F26B17/10F26B17/103F26B25/007
    • The present invention relates to a device for removing fluids and/or solid substances from a mixture of particle-shaped materials with a container which forms a ring-shaped process chamber with a plurality of cells separated from each other by walls, comprising an inlet cell, intermediate cells and an outlet cell, a feeding installation for conveying the mixture to be treated into the inlet cell of the process chamber, a discharge installation for discharging the mixture treated from the outlet cell of the process chamber, a ventilation installation for feeding in a first fluidisation agent, in particular in the form of overheated vapour, from below into the process chamber through an inflow floor for generating a fluidised bed in the process chamber, a heating installation for preparing the first fluidisation agent in the flow direction before the ventilation installation, swirl impellers for conditioning the flow in the container from the process chamber to the heating installation and which in part also leads to a vapour outlet, and a dust removal installation in the flow path between the process chamber and the heating installation, wherein dust can be guided to the outlet cell via the dust removal installation, wherein in order to support a transportation of the mixture from the inlet cell to the outlet cell and/or a turbulence of the mixture in the process chamber, the inflow floor comprises first unevenness and/or at least at times a second fluidisation agent, in particular in the form of overheated vapour, can be fed at least into the inlet cell essentially parallel to the inflow floor by means of first nozzles, and/or first flow guidance members are provided above the inflow floor and/or second flow guidance members are provided below the inflow floor.
    • 本发明涉及一种用于从颗粒状材料的混合物中除去流体和/或固体物质的装置,该容器形成具有通过壁彼此分离的多个细胞的环状处理室,该容器包括入口池 中间单元和出口单元,用于将要处理的混合物输送到处理室的入口单元的进料装置,用于排出从处理室的出口单元处理的混合物的排出装置,用于进料的通风装置 第一流态化剂,特别是过热蒸汽的形式,从下面通过流入底板进入处理室,用于在处理室中产生流化床;加热装置,用于在通风之前沿流动方向准备第一流化剂 安装,旋转叶轮,用于调节容器中从处理室到加热装置的流动 其部分地还导致蒸气出口,以及在处理室和加热装置之间的流动路径中的除尘装置,其中灰尘可以经由除尘装置被引导到出口单元,其中为了支撑 混合物从入口池输送到出口池和/或处理室中的混合物的湍流,流入地板包括第一不均匀性和/或至少有时第二流化剂,特别是过热形式 蒸气可以通过第一喷嘴至少基本上平行于入流底板进入入口单元,和/或第一流动引导构件设置在流入地板的上方,和/或第二流动引导构件设置在流入地板的下方。
    • 6. 发明申请
    • VERFAHREN ZUR GEWINNUNG VON KRISTALLEN AUS EINER MUTTERLÖSUNG UND DAFÜR GEEIGNETER KRISTALLISATIONSAPPARAT
    • 从螺母溶液中获得晶体的方法和适合于此的晶体化装置
    • WO2017129590A1
    • 2017-08-03
    • PCT/EP2017/051493
    • 2017-01-25
    • BMA BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG
    • MAHRHOLZ, JensLEHNBERGER, Andreas
    • C13B30/02B01D9/00
    • C13B30/025B01D9/0036B01D9/0063C13B30/027
    • Ein Verfahren zur Gewinnung von Kristallen aus einer Mutterlösungarbeitet damit, dass Mutterlösung in einen Kristallisationsapparat gegeben wird. Durch Steuerung und/oder Regelung der Temperatur () wird eine Übersättigung der Mutterlösung herbeigeführt. Saatkristalle werden an einem Saatpunkt (Sp) der Mutterlösung hinzugefügt. Durch kontinuierliche Prozessregelung werden die Saatkristalle als Keime vergrößert und schließlich als Kristalle aus dem Verfahren entnommen. Sie bilden die Produktausbeute. Der Bildung von Kristallkeimen in der Mutterlösung wird durch Schritte in der Prozessregelung entgegengewirkt. Eine Ermittlung der Lage der Grenze(M)der Bildung von Sekundärkeimen erfolgtwährend der Prozessregelung und des Kristallisationsvorgangs mittels Sensoren, die aktuell Daten erfassen, wobei aus diesen Daten die Lage der Grenze (M) als Wert der Konzentration (c) und der Temperatur ()erfolgt. Diese ermittelte Lage der Grenze (M) der Bildung von Kristallkeimen wird für die Prozessregelung der Kristallisation herangezogen.
    • 从母液中回收晶体的方法是通过将母液加入结晶器中进行操作。 通过控制和/或调节温度(),实现母液的调和。 晶种在晶种点(Sp)加入到母液中。 通过连续的过程控制,晶种作为晶种被扩大并最终作为晶体从过程中去除。 它们形成产品收益率。 过程控制中的步骤抵消母液中核的形成。 边界(M)副BEAR的形成的位置的确定rkeimen erfolgtwÄ而过程控制和借助于传感器的结晶过程中,当前检测的数据,从该数据中,边界的(M)作为浓度(C)的值的位置和 温度()发生。 该确定的晶核形成边界(M)的位置用于结晶的过程控制。
    • 10. 发明授权
    • Fluidized-bed vaporisation dryer
    • US10330385B2
    • 2019-06-25
    • US15307716
    • 2015-03-09
    • BMA BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG
    • Gerald CaspersHartmut HafemannCarsten BonathHolger Fersterra
    • F26B3/08F26B17/10F26B25/00
    • The present invention relates to a device for removing fluids and/or solid substances from a mixture of particle-shaped materials with a container which forms a ring-shaped process chamber with a plurality of cells separated from each other by walls, comprising an inlet cell, intermediate cells and an outlet cell, a feeding installation for conveying the mixture to be treated into the inlet cell of the process chamber, a discharge installation for discharging the mixture treated from the outlet cell of the process chamber, a ventilation installation for feeding in a first fluidisation agent, in particular in the form of overheated vapour, from below into the process chamber through an inflow floor for generating a fluidised bed in the process chamber, a heating installation for preparing the first fluidisation agent in the flow direction before the ventilation installation, swirl impellers for conditioning the flow in the container from the process chamber to the heating installation and which in part also leads to a vapour outlet, and a dust removal installation in the flow path between the process chamber and the heating installation, wherein dust can be guided to the outlet cell via the dust removal installation, wherein in order to support a transportation of the mixture from the inlet cell to the outlet cell and/or a turbulence of the mixture in the process chamber, the inflow floor comprises first unevenness and/or at least at times a second fluidisation agent, in particular in the form of overheated vapour, can be fed at least into the inlet cell essentially parallel to the inflow floor by means of first nozzles, and/or first flow guidance members are provided above the inflow floor and/or second flow guidance members are provided below the inflow floor.