REACTIVE DISTILLATION APPARATUS FOR A MULTISTAGE COUNTER-CURRENT ROTATING BED AND ITS APPLICATION

    公开(公告)号:US20110214979A1

    公开(公告)日:2011-09-08

    申请号:US12990454

    申请日:2010-06-12

    IPC分类号: B01D3/08

    CPC分类号: B01D3/009

    摘要: The present invention discloses a reactive distillation apparatus for multistage counter-current rotating bed and its application, the apparatus comprises a closed shell, in the center of which a revolving shaft linking each shell section is set, the said shaft is provided with two or more rotors in series connection, a feeding inlet, a reflux inlet and an outlet of the gas phase are mounted on the top end face of the shell while a waste liquid outlet and an inlet of the gas phase are set on the bottom end face of the shell, the said shell consists of an upper section of the shell and a lower section of the shell along the axial direction, the said rotor consists of a rotating disc firmly connecting with the revolving shaft and a static disc mounted to the shell, a group of concentric dynamic filler rings but with different diameters are installed at intervals along the radial direction, wherein the wall of the dynamic filler rings is holed, and the ring clearance between the dynamic filler rings is configured with static rings fastened on the static disc; the filler filled in the said dynamic filler ring includes a catalytic filler and a wire gauze filler with the catalyst filler filled in the dynamic filler ring of the outer circle of the upper rotor and the inner circle of the lower rotor and the wire gauze filler filled in the rest of the dynamic filler rings, to make the whole rotor structure equivalent to the distillation section, reactive distillation section and stripping section; a feeding inlet is arranged on the top cover of the shell corresponding to the spray nozzle of raw material liquid; a rotating liquid distributor is arranged on the inner side of the innermost dynamic filler ring of the said lower rotor. The catalyst of the present invention not only plays the role of catalytic reaction, but also increases the interphase mass transfer area; the present invention improves the mass transfer efficiency and the separation efficiency of the reactive distillation process.

    Reactive distillation apparatus for a multistage counter-current rotating bed and its application
    2.
    发明授权
    Reactive distillation apparatus for a multistage counter-current rotating bed and its application 有权
    多级逆流旋转床反应蒸馏装置及其应用

    公开(公告)号:US08551295B2

    公开(公告)日:2013-10-08

    申请号:US12990454

    申请日:2010-06-12

    IPC分类号: B01D3/00 B01J4/00 B01J8/02

    CPC分类号: B01D3/009

    摘要: A reactive distillation apparatus for multistage counter-current rotating bed includes a closed shell, in the center of which a revolving shaft linking each shell section is set, the shaft is provided with two or more rotors in series connection, a feeding inlet, a reflux inlet and an outlet of the gas phase are mounted on the top end face of the shell while a waste liquid outlet and an inlet of the gas phase are set on the bottom end face of the shell, a group of concentric dynamic filler rings with different diameters are installed at intervals along the radial direction, wherein the wall of the dynamic filler rings is holed, and the ring clearance between the dynamic filler rings is configured with static rings fastened on the static disc; a feeding inlet is arranged on the top cover of the shell corresponding to the spray nozzle of raw material liquid; a rotating liquid distributor is arranged on the inner side of the innermost dynamic filler ring of the said lower rotor.

    摘要翻译: 一种用于多级逆流旋转床的反应性蒸馏装置,包括封闭的壳体,其中心设置有连接每个壳体部分的旋转轴,该轴设置有两个或更多个串联的转子,进料口,回流 气相的入口和出口安装在壳体的顶端面上,而废液出口和气相入口设置在壳体的底端面上,一组具有不同的同心动态填料环 直径沿径向方向间隔地安装,其中动态填充环的壁是开孔的,并且动态填充环之间的环间隙被构造成固定在静态盘上的静环; 在与原料液喷雾喷嘴相对应的壳体顶盖上设有进料口; 旋转液体分配器布置在所述下转子的最内部动态填充环的内侧。

    METHOD FOR SYNTHESIS OF BUTYL RUBBER
    3.
    发明申请
    METHOD FOR SYNTHESIS OF BUTYL RUBBER 有权
    合成丁基橡胶的方法

    公开(公告)号:US20090286948A1

    公开(公告)日:2009-11-19

    申请号:US12307121

    申请日:2007-07-20

    IPC分类号: C08F236/08

    摘要: This invention puts forward a process of preparing butyl rubber. High gravity devices are used as polymerization reactor. The mixture of isomonoolefin and conjugated diolefin monomers and the diluent, and the mixture of the initiator and diluent are pumped at a certain ratio into a high-gravity reactor to conduct cationic polymerization in the high-gravity environment. After polymerization, the monomers and the diluent are removed from the product to obtain butyl rubber polymers with number-average molecular weight of 80000˜300000 and molecular weight distribution index of 1.9˜3.6. The high gravity polymerization method of this invention can tremendously intensify micro-mixing, mass transfer and heat transfer in the reaction. Compared to the conventional stirred polymerization method, this invention features small reactor volume, at least 30-fold shorter residence time of substances in the high gravity reactor, low cost, low energy consumption and high production efficiency.

    摘要翻译: 本发明提出了制备丁基橡胶的方法。 高重力装置用作聚合反应器。 将异麦烯烃和共轭二烯烃单体和稀释剂的混合物,引发剂和稀释剂的混合物以一定的比例泵送到高重力反应器中以在高重力环境中进行阳离子聚合。 聚合后,从产物中除去单体和稀释剂,得到数均分子量为80000〜300000,分子量分布指数为1.9〜3.6的丁基橡胶聚合物。 本发明的高重力聚合方法可以极大地加强反应中的微混合,传质和传热。 与常规的搅拌聚合方法相比,本发明具有反应器体积小,物料在高重力反应器中停留时间缩短至少30倍,成本低,能耗低,生产效率高的优点。

    Method for synthesis of butyl rubber
    4.
    发明授权
    Method for synthesis of butyl rubber 有权
    丁基橡胶的合成方法

    公开(公告)号:US07776976B2

    公开(公告)日:2010-08-17

    申请号:US12307121

    申请日:2007-07-20

    摘要: This invention puts forward a process of preparing butyl rubber. High gravity devices are used as polymerization reactor. The mixture of isomonoolefin and conjugated diolefin monomers and the diluent, and the mixture of the initiator and diluent are pumped at a certain ratio into a high-gravity reactor to conduct cationic polymerization in the high-gravity environment. After polymerization, the monomers and the diluent are removed from the product to obtain butyl rubber polymers with number-average molecular weight of 80000˜300000 and molecular weight distribution index of 1.9˜3.6. The high gravity polymerization method of this invention can tremendously intensify micro-mixing, mass transfer and heat transfer in the reaction. Compared to the conventional stirred polymerization method, this invention features small reactor volume, at least 30-fold shorter residence time of substances in the high gravity reactor, low cost, low energy consumption and high production efficiency.

    摘要翻译: 本发明提出了制备丁基橡胶的方法。 高重力装置用作聚合反应器。 将异麦烯烃和共轭二烯烃单体和稀释剂的混合物,引发剂和稀释剂的混合物以一定的比例泵送到高重力反应器中以在高重力环境中进行阳离子聚合。 聚合后,从产物中除去单体和稀释剂,得到数均分子量为80000〜300000,分子量分布指数为1.9〜3.6的丁基橡胶聚合物。 本发明的高重力聚合方法可以极大地加强反应中的微混合,传质和传热。 与常规的搅拌聚合方法相比,本发明具有反应器体积小,物料在高重力反应器中停留时间至少缩短30倍,成本低,能耗低,生产效率高的优点。