Process for the manufacture of halogenated polymers
AssigneeExxon Research & Engineering Co.
InventorsRonald C. Kowalski, William M. Davis, Neil F. Newman, Lewis Erwin
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AssigneeExxon Research & Engineering Co.
InventorsRonald C. Kowalski, William M. Davis, Neil F. Newman, Lewis Erwin
Estimating the term…
Continuous halogenation of polymers is achieved by contacting polymer and halogenating agent in a continuous flow device in which the reactants are present as either co-continuous phases or wherein the halogenating agent is present as a continuous phase and the polymer is present as a discontinuous phase, the polymer is subjected to deformation during reaction and in which means are provided for disengaging reaction by-products and unreacted halogenating agent from the reaction mixture. In a preferred embodiment the polymer passes through three extruder-reactor zones under controlled conditions to achieve halogenation: feed, reaction (preferably vented), neutralization, and optionally a wash and exit zone. A continuous halogenating agent phase is achieved during reaction by avoiding complete filling of the reaction zone with polymer. Various halogenated polymers are produced, for example, halogenated linear low density polyethylene and halogenated butyl rubber.
A process for the continuous production of halogenated polymer wherein polymer and halogenating agent are contacted in a continuous flow device comprising means for conveying said polymer through said device wherein said polymer and said halogenating agent are present during contact as either co-continuous phases or wherein said halogenating agent is present as a continuous phase and said polymer is present as a discontinuous phase and said polymer is subject to deformation, disruption and generation of new surface and means for disengaging by-product of the halogenation reaction and unreacted halogenating agent from said halogenated polymer.
A process for the continuous production of halogenated polymer by reacting said polymer and a halogenating agent in an extruder-reactor, said extruder-reactor comprising feed zone (A), reaction zone (B) and neutralization zone (C) in sequence;
Dependencies are inferred from the claim text.