Control over controlled radical polymerization processes
AssigneeATRP Solutions, Inc.
InventorsWojciech Jakubowski, James Spanswick
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Abstract
A procedure for improved temperature control in controlled radical polymerization processes is disclosed. The procedure is directed at controlling the concentration of the persistent radical in ATRP and NMP polymerizations procedures and the concentration of radicals in a RAFT polymerization process by feeding a reducing agent or radical precursor continuously or intermittently to the reaction medium through one of more ports.
Claims20
A method for safely operating a fast large-scale ICAR ATRP polymerization process, comprising:
- (a) mixing an unsaturated monomer, an initiator, optionally ligand and a metal catalyst;
- (b) adding a non-activated reducing agent;
- and
- (c) maintaining the polymerization process at or above conditions wherein the non-activated reducing agent has an activation-dependent t112 value of between 30 sec. and 30 min.
A method of polymerizing unsaturated monomers, comprising:
- (a) mixing unsaturated monomers with an inactive metal catalyst, optionally ligand and an initiator having a transferable atom, wherein the inactive metal catalyst is present in the mixture at an amount of less than 250 ppm, on a mass basis relative to the total mixture;
- (b) heating the mixture to a reaction temperature;
- (c) adding a first portion of a non-activated reducing agent to the system to generate an activated reducing agent, wherein the non-activated reducing agent has a decomposition activation-dependent t1/2 value of between 30 sec. and 30 min. at at least one of the reaction conditions;
- (d) reducing the inactive metal catalyst with the activated reducing agent to form an active metal catalyst;
- (e) transferring the transferable atom with the active metal catalyst, thereby activating the initiator for unsaturated monomer addition;
- and
- (f) adding at least a further portion of the non-activated reducing agent to the mixture to induce further polymerization of the unsaturated monomer;
- wherein the at least further portion is added to the mixture at a point where at least 30 molar %, relative to the amount of unsaturated monomer introduced into the mixture, has been polymerized, and
- wherein at least one polymer product has a degree of polymerization, with respect to the monomer residues corresponding to the unsaturated monomer, of at least 20 and the overall mixture has a conversion of at least 60 molar % relative to the amount of unsaturated monomer introduced into the mixture.
A method of radical polymerization of an unsaturated monomer, comprising:
- (a) polymerizing an unsaturated monomer in a system comprising an initiator, optionally ligand and a metal catalyst at or above a reaction temperature;
- (b) adding at a controlled rate a first amount of non-activated reducing agent to the system;
- and
- (c) controlling the rate of polymerization of the unsaturated monomer by adding at a controlled rate a further amount of the non-activated reducing agent to the system at a point where at least 30 molar %, relative to the amount of unsaturated monomer introduced into the system, has been polymerized;
- wherein at least one reaction conditions is at or above a point suitable to trigger the decomposition of the non-activated reducing agent to form an active reducing agent.
A method of making a polymer, comprising:
- (a) preparing a reaction mixture comprising a radically-polymerizable unsaturated monomer, an initiator, optionally ligand and an inactive metal catalyst in a molar ratio of the unsaturated monomer to the initiator of 25-5000:1 and a molar ratio of the catalyst to the initiator of 0.001 to 0.5:1 and the inactive metal catalyst is present in the mixture at an amount of less than 250 ppm, on a mass basis relative to the total mixture;
- (b) heating the reaction mixture to a first temperature;
- (c) disbursing a portion of a thermo-activated reducing agent into the heated reaction mixture;
- (d) allowing a quantity of said portion of the thermo-activated reducing agent to decompose to an activated reducing agent;
- (e) reducing a portion of the inactive metal catalyst with a portion of the activated reducing agent to form at least one active metal catalyst;
- (f) activating one or more of the initiators with the at least one active metal catalyst to form one or more activated initiators;
- (g) polymerizing at least one monomer in the presence of one or more activated initiators to extend a polymer chain;
- and
- (h) repeating steps (c)-(g) while maintaining the temperature at or above a second temperature;
- wherein the first and second temperatures are at or above a temperature wherein the thermo-activated reducing agent has a temperature-dependent t1/2 value of between 30 sec. and 30 min.
Dependencies are inferred from the claim text.