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    • 3. 发明授权
    • Process and apparatus for the agglomeration of hydrolytically sensitive
substances by means of steam
    • 通过蒸汽凝结水解敏感物质的方法和设备
    • US5955036A
    • 1999-09-21
    • US240033
    • 1999-01-29
    • Ina SeyffertHans UhlemannReinhardt WalterJoachim Martin Maasz
    • Ina SeyffertHans UhlemannReinhardt WalterJoachim Martin Maasz
    • B01J2/16A61K9/16B01J2/04B01J2/28C08F5/02B05D7/00
    • A61K9/1694B01J2/04B01J2/16
    • In the process for the agglomeration of slightly soluble and hydrolytically sensitive substances, a powder of the slightly soluble substance is conducted, together with at least one water-soluble binder, in free fall through a steam atmosphere at temperatures between 85.degree. C. and 105.degree. C. essentially without the action of compacting forces. In this process, the residence time in the steam atmosphere is approximately 0.5 to 10 seconds. The agglomerates formed are then dried in free fall, so that small solid bridges form from the binder liquid bridges formed at the points of contact between the primary particles. In a following integrated fluidized-bed dryer, the final drying then takes place to a water content of less than 0.5% by weight. The process is carried out in a steam jet agglomerator in which a freely falling product curtain of the pulverulent mixture to be agglomerated is impinged by steam using steam jet nozzles (5, 6). A fluidized-bed dryer (2) is connected at the lower part of the agglomerator (1) in such a manner that the agglomerated particles (4) fall directly into the fluidized bed.
    • 在微溶性和水解敏感性物质结块的过程中,将微溶性物质的粉末与至少一种水溶性粘合剂一起在85℃至105℃的温度自由落体通过蒸汽气氛 基本上没有压实力的作用。 在该方法中,在蒸气气氛中的停留时间为约0.5〜10秒。 然后形成的附聚物在自由落体下干燥,从而在形成于初级颗粒之间的接触点处的粘合剂液体桥形成小的固体桥。 在随后的集成流化床干燥器中,最后的干燥发生到小于0.5重量%的含水量。 该方法在蒸汽喷射附聚器中进行,其中待凝聚的粉状混合物的自由落下的产品帘幕使用蒸汽喷嘴(5,6)被蒸汽冲击。 流化床干燥器(2)以附聚颗粒(4)直接落入流化床的方式连接在附聚器(1)的下部。
    • 5. 发明授权
    • Process and device for fluidized bed spray granulation
    • 流化床喷雾造粒工艺及装置
    • US5213820A
    • 1993-05-25
    • US714357
    • 1991-06-12
    • Hans UhlemannReinhard BoeckHans DaunHeiko Herold
    • Hans UhlemannReinhard BoeckHans DaunHeiko Herold
    • B01J2/16B07B4/04
    • B01J2/16B07B4/04
    • Granule production is based on particle growth in a fluidized bed (4), in which the liquid starting product is sprayed into the fluidized bed and the finished granular particle is discharged from the fluidized bed (4) with classification. The classification is carried out with the aid of a classifying air flow which is divided into individual single flows (6) to each of which is assigned a zigzag classifier module (7, 17) and a spray nozzle (5) or a group of spray nozzles. The course of the classifying process is such that the granular particles which are too small and have not yet reached the desired diameter are thrown back into the fluidized bed (4) by a return shaft (9, 18) seated on each of the zigzag classifier modules (7, 17) in parallel or radial zones without cross-mixing, in which the relatively small particles impinge at a relatively large distance from the return shaft (9, 18) and the large particles, which have already grown close to the discharge size, impinge at a relatively small distance. The process is carried out with the aid of a fluidized bed granulator, to the inlet plate (2) of which is connected a zigzag classifier, subdivided in a modular manner, in which each zigzag classifier module (7, 17) is provided with a return shaft (9, 18) at the point where it joins the inlet plate (2, 16). In addition, at least one spray nozzle (5) at the inlet plate (2, 16) is allocated to each zigzag classifier module (7, 17).
    • 颗粒生产基于流化床(4)中的颗粒生长,其中将液体起始产物喷射到流化床中,并且成品粒状颗粒从分级流出床(4)排出。 分类是借助于划分为单独的单个流(6)的分类空气流进行的,每个流被分配有锯齿形分类器模块(7,17)和喷嘴(5)或一组喷雾 喷嘴。 分级过程的过程是使得太小并且尚未达到期望直径的粒状颗粒通过位于每个锯齿形分级器上的返回轴(9,18)被抛回到流化床(4)中 模块(7,17)在没有交叉混合的情况下处于平行或径向区域,其中相对较小的颗粒以相对较大的距离离开返回轴(9,18)和已经生长在接近放电的大颗粒 尺寸,在相对较小的距离处撞击。 借助于流化床造粒机进行该过程,其入口板(2)连接有以模块方式细分的锯齿形分类器,其中每个锯齿形分类器模块(7,17)设置有 在其连接入口板(2,16)的位置处的返回轴(9,18)。 此外,入口板(2,16)处的至少一个喷嘴(5)被分配给每个锯齿形分类器模块(7,17)。