Rotor and stirring device
    1.
    发明授权

    公开(公告)号:US10384177B2

    公开(公告)日:2019-08-20

    申请号:US15320442

    申请日:2015-08-12

    Abstract: The present invention relates to a rotor that comprises a series of shaped rotor blades whose circumferential section forms a standard NACA four-digit airfoil. Said rotor can be inserted in a stirring device that also comprises a stator, on whose inner surface shaped stator blades are positioned, whose circumferential section forms a standard NACA four-digit airfoil.

    REACTION CONFIGURATION AND PROCEDURE FOR POLYMERS PRODUTION

    公开(公告)号:US20220267482A1

    公开(公告)日:2022-08-25

    申请号:US17252013

    申请日:2019-06-11

    Abstract: There is a procedure for polymerisation in solution for the production of polymers. The procedure has the following steps: (A) continuously feeding one or more monomers, one or more solvents in a quantity comprised between 70% and 90% by weight with respect to the reagent mixture, and a catalytic system, to a first stirred reaction volume, wherein a single mixing cell is formed, in which the polymerisation begins, until a conversion is attained that varies from 20% to 70% with respect to the final conversion achieved and (B) proceeding the polymerisation in at least one second stirred reaction volume connected in series to the first reaction volume, in which two or more mixing cells are formed, at the outlet of which the final conversion of the monomer is attained. In the first reaction volume, the average residence time of the reagent mixture varies within an interval ranging from 10% to 25% with respect to the average residence time of the entire reaction volume.

    Energy Recovery System and Method and Polymerization Plant with Such a Recovery System
    3.
    发明申请
    Energy Recovery System and Method and Polymerization Plant with Such a Recovery System 有权
    能量回收系统和方法与聚合工厂的回收系统

    公开(公告)号:US20150338172A1

    公开(公告)日:2015-11-26

    申请号:US14427788

    申请日:2013-10-22

    Abstract: The present invention relates to a system for energy recovery and a polymerization plant having such a system comprising a. an exothermic device operating continuously (exothermic device interpreted as any apparatus able to produce heat and transfer it onto another body), b. a cooling device in fluid communication with said exothermic device, c. an endothermic device operating discontinuously (endothermic device interpreted as any apparatus able to receive heat from another body, i. e. to be heated); said system being characterized in that it comprises a device for the accumulation of the energy produced by the exothermic device in fluid communication with the discontinuous endothermic device, the exothermic device operating continuously and the cooling device using a service fluid.

    Abstract translation: 本发明涉及一种能量回收系统和具有这种系统的聚合装置,该系统包括:a。 放热装置连续工作(放热装置被解释为能够产生热量并将其转移到另一身体上的任何装置),b。 与所述放热装置流体连通的冷却装置,c。 吸热装置不连续地操作(吸热装置被解释为能够从另一个身体接收热量的任何装置,即被加热); 所述系统的特征在于,其包括用于累积由不连续吸热装置流体连通的放热装置产生的能量的装置,连续工作的放热装置和使用工作流体的冷却装置。

    Reaction configuration and procedure for polymers production

    公开(公告)号:US11834530B2

    公开(公告)日:2023-12-05

    申请号:US17252013

    申请日:2019-06-11

    CPC classification number: C08F2/01 C08F2/06

    Abstract: There is a procedure for polymerisation in solution for the production of polymers. The procedure has the following steps: (A) continuously feeding one or more monomers, one or more solvents in a quantity comprised between 70% and 90% by weight with respect to the reagent mixture, and a catalytic system, to a first stirred reaction volume, wherein a single mixing cell is formed, in which the polymerisation begins, until a conversion is attained that varies from 20% to 70% with respect to the final conversion achieved and (B) proceeding the polymerisation in at least one second stirred reaction volume connected in series to the first reaction volume, in which two or more mixing cells are formed, at the outlet of which the final conversion of the monomer is attained. In the first reaction volume, the average residence time of the reagent mixture varies within an interval ranging from 10% to 25% with respect to the average residence time of the entire reaction volume.

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