Process to produce fluoropolymer-based latex with mechanical stability

Patent metadata

Field	Value
Publication number	US-10414879-B2
Application number	US-201615564869-A
Country	US
Kind code	B2
Filing date	Apr 4, 2016
Priority date	Apr 7, 2015
Publication date	Sep 17, 2019
Grant date	Sep 17, 2019

Abstract

The present disclosure relates to a polymerization process wherein the emulsifier is introduced in an initial batch as well as during a continuous feed to provide improved mechanical stability of the generated latex. Improved soap coverage can also be achieved during the polymerization process.

First claim

What is claimed:

1. A polymerisation process comprising:
charging an initial charge of reagents to a reaction vessel and a subsequent feed of reagents to the reaction vessel, wherein the initial charge comprises a polytetrafluoroethylene dispersion, water, a portion of a predetermined amount of monomers and a portion of a predetermined amount of tallow fatty acid soap heated to an appropriate temperature and allowed to pre-condition for a duration of time prior and the subsequent feed comprises an initiator, a remaining portion of the predetermined amount of monomers and a remaining portion of the predetermined amount of tallow fatty acid soap.

2. The process according to claim 1 , wherein the monomers are styrene and acrylonitrile.

3. The process according to claim 1 , wherein the contents of the reaction vessel are allowed to pre-condition for at least 15 minutes prior to the charging of the subsequent feed of reagents.

4. The process according to claim 1 , wherein the temperature of the contents of the vessel is raised during the charging of the subsequent feed of reagents.

5. The process according to claim 1 , wherein the temperature of the contents of the vessel is between 54.4° C. (130° F.) and 71.1° C. (160° F.).

6. The process according to claim 1 , wherein the initiator is a combination of cumene hydroperoxide, ferrous sulfate, tetrasodium pyrophosphate and a reducing sugar.

7. The process of claim 2 wherein a poly(tetrafluoroethylene)-styrene-acrylonotrile resin is formed further comprising a coagulation process to isolate the poly(tetrafluoropolyethylene-styrene-acrylonitrile) resin.

8. The process of claim 7 wherein the coagulation comprises the addition of an acid and water to the latex resulting from the polymerisation reaction.

9. The process of claim 7 wherein the isolated poly(tetrafluoropolyethylene-styrene-acrylonitrile) resin is dried upon isolation.

10. The process of claim 1 wherein the polytetrafluoroethylene is present in an amount of 45 to 55 parts by weight, the portion of the predetermined amount of monomers in the initial charge is from 1 to 20 parts by weight and the portion of the predetermined amount of tallow fatty acid soap in the initial charge is less than 1.75 parts by weight.

11. The process of claim 1 wherein the initial charge does not include activator and an activator is present in the subsequent feed.

12. The process of claim 1 wherein the portion predetermined amount of monomer is either styrene or acrylonitrile in an amount of 1 to 20 parts by weight.

13. A process, wherein the process comprises:
a. an initial charge comprising:
introducing an aqueous dispersion of polytetrafluoroethylene into a vessel;
introducing a styrene or acrylonitrile monomer into the vessel;
introducing a soap into the vessel;
heating the contents of the vessel to between 54.4° C. (130° F.) to 60° C. (140° F.); and
allowing the dispersion to precondition in the vessel for 15 minutes;
wherein the initial charge comprises introducing 45 parts by weight to 55 parts by weight of polytetrafluoroethylene, 1 to 20 parts by weight of the styrene or acrylonitrile monomer, and 0.5 part by weight to 5 parts by weight of the soap into the vessel;
b. after a., a continuous feed comprising:
introducing styrene and acrylonitrile monomers;
introducing a redox initiator system;
introducing a soap; and
heating the contents of the vessel to between 65.6° C. (150° F.) to 71.1° C. (160° F.) when approximately fifty percent by weight of the styrene monomer, the acrylonitrile monomer, are introduced into the vessel,
wherein the continuous feed comprises 31 parts by weight to 34 parts by weight of styrene monomer, 11 parts by weight to 14 parts by weight of acrylonitrile introduced over a period of time from 1 hour to 2.5 hours, 0.1 to 2 parts by weight redox initiator system, and from 1 part by weight to 5 parts by weight of soap; and
wherein the polymerisation process produces a styrene-acrylonitrile copolymer encapsulated polytetrafluoroethylene latex dispersion;
and
c. coagulating the styrene-acrylonitrile copolymer encapsulated polytetrafluoroethylene latex dispersion, wherein the latex is exposed to a heated mixture of water and a coagulant to produce an output slurry.

Assignees

• Sabic Global Technologies Bv

Inventors

• Lowry Vern
• Chang Yin-Shen

Classifications

• C08F259/08 Primary

  on to polymers containing fluorine · CPC title

• C08F2/26 Primary

  anionic · CPC title

• C08F2/24

  with the aid of emulsifying agents · CPC title

• C08J3/16 Primary

  by coagulating dispersions {(C08J3/122 takes precedence)} · CPC title

• C08J3/05

  from solid polymers · CPC title