Process for polymerizing or copolymerizing ethylenically unsaturated monomers in the presence of free-radical polymerization initiators at pressures in the range of from 110 MPa to 500 MPa and temperatures in the range of from 100°C to 350°C in a continuously operated polymerization apparatus, wherein the reaction gas composition is compressed to the polymerization pressure by at least two sequentially operating compressors in which a low-pressure compressor first compresses the reaction gas composition to a pressure of from 10 MPa to 50 MPa and a high-pressure compressor then further compresses the reaction gas composition to the polymerization pressure wherein the high-pressure compressor is operated with a polyalkylene glycol based synthetic lubricant and oxygen is introduced into the fresh gas feed or into the polymerization apparatus in an amount that the gas composition to be compressed in the high-pressure compressor has an oxygen content in the range of from 0.01 ppm to 0.9 ppm and
process for operating a compressor for pressurizing ethylenically unsaturated monomers to a pressure of from 5 MPa to 500 MPa in which the compressor is lubricated with a polyalkylene glycol based synthetic lubricant and the gas composition to be pressurized has an oxygen content in the range of from 0.01 ppm to 0.9 ppm.
在连续操作的聚合装置中,在自由基聚合
引发剂存在下,在压力为 110 兆帕至 500 兆帕,温度为 100℃至 350℃的范围内,使
乙烯基不饱和单体聚合或共聚合的工艺、其中,反应气体组合物被至少两个顺序运行的压缩机压缩至聚合压力,其中低压压缩机首先将反应气体组合物压缩至 10 兆帕至 50 兆帕的压力,然后高压压缩机进一步将反应气体组合物压缩至聚合压力,其中高压压缩机采用烷基烃压缩机运行。其中,高压压缩机使用聚亚烷基二醇基合成润滑剂运行,
氧气被引入新鲜气体进料或聚合设备中,引入量为高压压缩机中要压缩的气体成分的氧含量在 0.01 ppm 至 0.9 ppm 之间。01 ppm 至 0.9 ppm,以及
用于将
乙烯基不饱和单体加压至 5 兆帕至 500 兆帕压力的压缩机的操作工艺,其中压缩机使用以聚烯二醇为基础的合成润滑剂进行润滑,待加压气体成分的氧含量范围为 0.01 ppm 至 0.9 ppm。