Polymerization of ethylene in stirred autoclave with cooled inner wall

Claim 1

In a process of polymerizing ethylene under free-radical initiating conditions and in continuous manner at pressure of at least about 500 atmospheres and temperatures between about 125° and about 325°C at which the exothermic reaction of addition polymerization of ethylene is sustained without decomposition in a stirred autoclave comprising a relatively thick sidewall capable of withstanding the reaction pressure and defining at least one polymerization reaction zone, said continuous manner comprising continuously feeding ethylene to the reaction zone while stirring the resulting polymerization reaction mixture therein and continuously removing therefrom a portion of the resulting polymerization reaction mixture and sustaining the polymerization reaction in a substantially steady state, the improvement wherein the polymerization reaction zone is bounded in part by a relatively thin heat conductive wall means having a first surface in contact with the polymerization reaction mixture contained in that zone and a second surface near to the first surface but separated therefrom by said heat conductive wall, the said heat conductive wall means being supported by the said autoclave sidewall and lying between said autoclave sidewall and the said polymerization reaction zone, the dimensions of said heat conductive wall means and said autoclave sidewall being thin and thick, respectively, relative to each other, and the process is carried out while passing a heat exchange fluid in contact with said second surface, said heat exchange fluid being at a temperature below that of the polymerization reaction mixture, thereby removing part of the heat generated by the exothermic polymerization reaction occurring in the reaction zone from the reaction mixture therein through the said heat conductive wall means to the said heat exchange fluid.