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METHOD FOR PRODUCING (CO) POLYMERS AT PHASE TRANSITIONS OF SUPERCRITICAL FLUIDS AND A DEVICE FOR ITS CARRYING OUT

机译:在超临界流体的相变过程中生产(co)聚合物的方法及其实施装置

摘要

1. A method of obtaining (co) polymers by continuous interaction of at least one monomer with an initiator, its derivatives or their combinations and, optionally, in the presence of a solvent and / or modifying additive, carried out in one or more reaction zones of a straight-through tubular reactor, while maintaining the reaction conditions in the indicated zones, with continuous distillation of the gas mixture containing predominantly unreacted monomer and the isolation of the (co) polymer, characterized in that first! a) separate supply of at least one current stream of monomer, of at least one current stream of solvent and, optionally, supply of current streams of initiator and / or modifying additive, said streams being fed with supercritical pressure of monomer and / or solvent, then! b) heating said stream of solvent, additionally heating said stream of monomer to at least the supercritical temperature of the monomer and / or solvent to form a supercritical fluid, then! c) combining said streams of monomer, solvent and, optionally, initiator and / or modifier in a jet mixer (5) with a linear velocity providing a pressure below the supercritical pressure of the monomer and / or solvent, during which at least partial transition occurs supercritical fluid into the gas phase, and the period of time during which said combination is carried out is substantially less than 1 second, preferably less than 0.1 second, then! d) in a once-through tubular reactor (6) sharply decrease the linearity
机译:1.一种通过至少一种单体与引发剂,其衍生物或它们的组合的连续相互作用并且任选地在溶剂和/或改性添加剂的存在下,在一个或多个反应中进行来获得(共)聚合物的方法。直管式反应器的两个反应区,同时保持主要包含未反应单体的气体混合物的连续蒸馏和(共)聚合物的分离,同时保持指定区域的反应条件,其特征在于! a)单独供应至少一种当前的单体流,至少一种当前的溶剂流,以及任选地,供应当前的引发剂和/或改性添加剂流,所述流以单体和/或溶剂的超临界压力进料, 然后! b)加热所述溶剂流,另外将所述单体流加热至至少单体和/或溶剂的超临界温度以形成超临界流体,然后! c)在射流混合器(5)中以线速度合并所述单体,溶剂和任选的引发剂和/或改性剂的流,其线速度提供低于单体和/或溶剂的超临界压力的压力,在此期间至少部分过渡当超临界流体进入气相时,进行所述结合的时间段基本上小于1秒,优选小于0.1秒,然后! d)在直通式管式反应器(6)中急剧降低线性度

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