FIELD: chemistry.
SUBSTANCE: invention relates to process of polymerisation or copolymerisation of ethylene-unsaturated monomers in presence of free-radical polymerisation initiators under pressure in the interval from 110 MPa to 500 MPa and temperatures in the range from 100°C to 350°C in apparatus of continuously proceeding polymerisation. Reaction gas mixture is compressed to polymerisation pressure by at least two successively operating compressors. Low-pressure compressor compresses reaction gas mixture to pressure from 10 MPa to 50 MPa. High-pressure compressor then compresses reaction gas mixture to polymerisation pressure parameter. High-pressure compressor operates with synthetic polyalkyleneglycol-based lubricating material. Oxygen is introduced into mechanism for fresh gas supply or into polymerisation installation in quantity providing oxygen content in the range 0.01-0.9 ppm in gas mixture, compressed in high-pressure compressor.
EFFECT: reduction of sediment formation in high-pressure compressor and provision of compressor operation with higher capacity with reduction of compressor vibration.
8 cl, 1 dwg, 2 ex
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