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Guidance on Safety/Health for Process Intensification including MS Design; Part II: Explosion Hazards

机译:工艺强化安全/健康指南,包括MS设计;第二部分:爆炸危险

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The implementation of process intensification by multiscale equipment will have a profound impact on the way chemicals are produced. The shift to higher space-time yields for partial oxidation processes using micro-designed reactors comprises the risk of having a permanent explosive atmosphere in the reaction section. In Part I, it was concluded that spontaneous reaction with hot spots can be presumed if highly exothermic reactions were performed and may cause ignition of an explosive atmosphere. The risk analysis of the situation, based on public information in the literature, leads to the conclusion that microreactors are inherently safe regarding the initiation and propagation of an explosion inside a microchannel by an uncontrolled reaction. The situation is the opposite when a propagating explosion enters the same micro-designed reactor from one of the outside openings. The external explosion may enter the micro-designed equipment and destroy it when the same starting conditions are present.
机译:通过多规模设备实施过程强化将对化学品的生产方式产生深远影响。对于使用微型设计的反应器进行部分氧化过程,向更高的时空产率转移,存在在反应段中具有永久爆炸性气氛的风险。在第一部分中,得出的结论是,如果进行了高放热反应,则可以推测出与热点的自发反应,并且可能引起爆炸性气氛的点燃。根据文献中的公共信息,对该情况进行风险分析,得出的结论是,微反应器对于不受控制的反应在微通道内爆炸的发生和传播具有内在的安全性。当正在传播的爆炸从一个外部开口进入同一微型设计的反应堆时,情况则相反。当存在相同的启动条件时,外部爆炸可能会进入微型设计的设备并将其摧毁。

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