申请人:MINNESOTA MINING AND MANUFACTURING COMPANY
公开号:EP0646557A1
公开(公告)日:1995-04-05
Direct fluorination of organics such as 1,8-dichlorooctane in tubular reactor system. Inert liquid containing organic feed is circulated through tubular reactor with fluorine gas for a time and at a temperature sufficient to yield fluorinated organic. Preferably, liquid and gas phases are separated from reactor product stream containing inert liquid, fluorinated organic, and any unreacted organic is recycled to turbulent mixing zone upstream of reactor in which fresh organic feed is added; and fluorine is added to recycle stream at end of mixing zone. Flow in tubular reactor is turbulent. Rate of organic feed and fluorine addition to process are independent of each other. Among process advantages are: Freon solvents not required; good control of reaction exotherm; and HF scavengers not required. Process useful for partial or complete fluorination.
在管式反应器系统中对有机物(如 1,8-二氯辛烷)进行直接氟化。含有有机进料的惰性液体与氟气一起在管式反应器中循环,循环时间和温度足以产生氟化有机物。液相和气相最好从含有惰性液体、氟化有机物的反应器产品流中分离出来,任何未反应的有机物都被循环到反应器上游的湍流混合区,在该混合区中加入新鲜的有机物进料;氟被加入混合区末端的循环流中。管式反应器中的流体为湍流。有机进料和氟加入工艺的速度是相互独立的。该工艺的优点包括不需要氟利昂溶剂;反应放热控制良好;不需要氟化氢清除剂。该工艺适用于部分或全部氟化。