Method for ethylene polymerization in a tubular reactor with reduced output
AssigneeBasell Polyolefine GmbH
InventorsDieter Littmann, Andre-Armand Finette, Hans Joachim Meinke
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AssigneeBasell Polyolefine GmbH
InventorsDieter Littmann, Andre-Armand Finette, Hans Joachim Meinke
Estimating the term…
Process for the preparation of ethylene homopolymers or copolymers in the presence of free-radical polymerization initiators at from 100° C. to 350° C. and pressures in the range of from 160 MPa to 350 MPa in a tubular reactor with at least two spatially separated initiator injection points, wherein injecting initiator rises the temperature of the reaction mixture in the reaction zone following the injection point, and the first initiator injection point of the tubular reactor is not provided with initiator or is provided with so little initiator that the temperature of the reaction mixture does not rise more than 20° C. in the first reaction zone and method for reducing the output of a high pressure tubular reactor for the homo- or copolymerization of ethylene in the presence of free-radical polymerization initiators with at least two initiator injection points, wherein feeding of free-radical polymerization initiator to the first initiator injection point is discontinued or reduced to a level that the temperature of the reaction mixture in the first reaction zone does not rise more than 20° C.
A process for the preparation of ethylene homopolymers or copolymers in the presence of free-radical polymerization initiators at from 100° C. to 350° C. and pressures in the range of from 160 MPa to 350 MPa in a tubular reactor with at least two spatially separated initiator injection points, wherein the injecting initiator raises the temperature of the reaction mixture in the reaction zone following the injection point, and
A method for reducing the output of a high pressure tubular reactor for the homo- or copolymerization of ethylene in the presence of free-radical polymerization initiators with at least two initiator injection points, the method comprising feeding of the free-radical polymerization initiator to the first initiator injection point is discontinued or reduced to a level that the temperature of the reaction mixture in the reaction zone following the first initiator injection point does not rise more than 20° C., the reaction mixture having a flow velocity.
Dependencies are inferred from the claim text.