Process for operating a continuous removal of a target product X in the form of fine crystals of the target product X
    5.
    发明授权
    Process for operating a continuous removal of a target product X in the form of fine crystals of the target product X 有权
    用于以目标产物X的细晶体的形式连续移除靶产物X的方法

    公开(公告)号:US08106240B2

    公开(公告)日:2012-01-31

    申请号:US12208559

    申请日:2008-09-11

    IPC分类号: C07C51/42

    摘要: A process for operating a continuous removal of a target product X in the form of fine crystals of a liquid phase P comprising the target product X and constituents other than the target product X by cooling suspension crystallization in the secondary chamber of an indirect heat exchanger to which liquid phase P flows continuously with simultaneous continuous flow through the primary chamber of the indirect heat exchanger with a coolant, and continuous withdrawal of a crystal suspension S having a degree of crystallization Y from the secondary chamber in two operating states I and II, wherein the coolant temperature is lower, the mass flow of liquid phase P is greater and the molar proportion of the constituents other than the target product X in the liquid phase P in operating state II is greater than in operating state I.

    摘要翻译: 通过在间接热交换器的二次室中冷却悬浮液结晶来操作以含有目标产物X和除了目标产物X的成分的液相P的细晶体的形式连续除去目标产物X的方法, 该液相P以连续的流动方式连续流过间接热交换器的主室,并具有冷却剂,并且在两个操作状态I和II中连续取出具有结晶Y的程度的结晶悬浮液, 冷却剂温度较低,液相P的质量流量较大,并且在运行状态II下的液相P中除目标产物X以外的成分的摩尔比例大于运行状态I.

    PROCESS FOR CONTINUOUSLY REMOVING A TARGET PRODUCT X IN THE FORM OF FINE CRYSTALS
    10.
    发明申请
    PROCESS FOR CONTINUOUSLY REMOVING A TARGET PRODUCT X IN THE FORM OF FINE CRYSTALS 有权
    在精细晶体形式下连续去除目标产品X的方法

    公开(公告)号:US20090076284A1

    公开(公告)日:2009-03-19

    申请号:US12209594

    申请日:2008-09-12

    IPC分类号: C07C51/43 C07C7/14 C07D207/04

    摘要: A process for continuously removing a target product X in the form of fine crystals from a liquid phase P comprising the target product X and constituents other than the target product X by cooling suspension crystallization in the secondary chamber, into which the liquid phase P flows continuously, of an indirect heat exchanger with simultaneous continuous flow of a coolant through the primary chamber of the indirect heat exchanger and continuous withdrawal of a crystal suspension S having a degree of crystallization Y from the secondary chamber, in which the degree of crystallization Y is adjusted on the basis of a heat balance conducted continuously with the aid of a process computer.

    摘要翻译: 从液相P连续除去来自包含目标产物X的液相P和除了目标产物X以外的成分的微晶形式的目标产物X的方法,通过冷却液相P连续流入的二次室中的悬浮液结晶 的间接热交换器,其通过间接热交换器的主室同时连续流动冷却剂,并且从二级室连续取出具有结晶度Y的晶体悬浮液S,其中结晶度Y被调节 基于在过程计算机的帮助下连续进行的热平衡。