CONTINUOUS EMULSION POLYMERIZATION PROCESS AND INITIATION SYSTEM
In a continuous emulsion polymerization process, at least one monomer, an aqueous phase, and at least two different redox initiators are added to a continuous polymerization reactor comprising a first zone and a second zone. At least one redox initiator is added to the first zone and at least one redox initiator is added to the second zone.
1 . A continuous emulsion polymerization process comprising:
adding at least one monomer, an aqueous phase, and at least two different redox initiators to a continuous tubular reactor comprising (1) a circulating loop section and (2) a secondary line section having one end connected to a discharge opening of the loop section and a polymer outlet at its other end; and
polymerizing the at least one monomer.
2 . The process of claim 1 , wherein each redox initiator comprises a reducing agent and an oxidizing agent.
3 . The process of claim 1 , wherein the at least two different redox initiators are added to the tubular reactor at different locations.
4 . The process of claim 2 , wherein at least one of the at least two different redox initiators is added to the circulating loop section of the tubular reactor.
5 . The process of claim 4 , wherein the reducing agent from at least one of the at least two different redox initiators is added to the secondary line section of the tubular reactor.
6 . The process of claim 4 , wherein oxidizing agent from at least one of the at least two different redox initiators is added to the secondary line section of the tubular reactor.
7 . The process of claim 2 , wherein at least one of the at least two different redox initiators is water soluble and at least one of the at least two different redox initiators is oil soluble.
8 . The process of claim 7 , wherein the water soluble initiator is added to the reactor upstream of where the oil soluble initiator is added.
9 . The process of claim 7 , wherein the oxidizing agent from the oil soluble redox initiator is added to the circulating loop section of the tubular reactor and the reducing agent from the oil soluble redox initiator is added to the secondary line section of the tubular reactor.
10 . The process of claim 7 , wherein the reducing agent from the oil soluble redox initiator is added to the circulating loop section of the tubular reactor and the oxidizing agent from the oil soluble redox initiator is added to the secondary line section of the tubular reactor.
11 . The process of claim 2 , wherein the oxidizing agent from at least one of the at least two different redox initiators is added directly to the monomer before adding to the tubular reactor.
12 . The process of claim 11 , wherein the reducing agent from at least one of the at least two different redox initiators is added to the aqueous phase before adding to the tubular reactor.
13 . The process of claim 1 , wherein the oxidizing agents for the at least two different redox initiators are chosen from the group consisting of tBHP and t-butyl peroxy 3,5,5-trimethylhexanoate and the reducing agents for the at least two different redox initiators are chosen from the group consisting of SMBS and SFS.
14 . The process of claim 1 , wherein the tubular reactor further comprises two or more inlets through which the at least two redox initiators can be supplied to the tubular reactor at either the circulating loop section or the secondary line section.
15 . The process of claim 1 , wherein the tubular reactor further comprises a pump for continuously circulating the at least one monomer within the circulating loop section under conditions to effect polymerization thereof.
16 . The process of claim 5 , wherein the at least one monomer and the aqueous phase are continuously fed to the reactor at substantially the same rate as the rate of discharge into the secondary line section.
17 . The process of claim 1 , wherein the secondary line section of the tubular reactor has a volume of less than twice the volume of the circulating loop section.
18 . The process of claim 1 , wherein the discharge rate and the circulation rate in the circulating loop section of the tubular reactor are balanced such as to result in a monomer content in the loop section of less than 12 wt. %.
19 . The process of claim 1 , wherein the mean residence time in the circulating loop section of the tubular reactor is 12 minutes or less.
20 . A continuous emulsion polymerization process comprising:
adding at least one monomer, an aqueous phase, and at least two different redox initiators to a continuous polymerization reactor comprising a first zone and a second zone; and
polymerizing the at least one monomer;
wherein at least one redox initiator is added to the first zone and at least one redox initiator is added to the second zone.