Rubbers with tunable levels of metal containing anti-agglomerants

Patent metadata

Field	Value
Publication number	US-10000632-B2
Application number	US-201415107495-A
Country	US
Kind code	B2
Filing date	Dec 22, 2014
Priority date	Dec 23, 2013
Publication date	Jun 19, 2018
Grant date	Jun 19, 2018

Abstract

The invention relates to an efficient process for the preparation and isolation of rubber particles formed in aqueous media having a tunable level of metal containing anti-agglomerants and rubber particles obtained thereby. The invention further relates to copolymer products comprising the same or derived therefrom.

First claim

The invention claimed is:

1. A process for the preparation of an aqueous slurry comprising a plurality of copolymer particles suspended therein, the process comprising:
contacting monomers comprising at least one isoolefin monomer and at least one multiolefin monomer in an organic diluent with an initiator system to polymerize the monomers to form copolymers in a medium comprising the copolymers, the organic diluent and optionally residual monomers;
contacting the copolymer medium with an aqueous medium comprising at least one lower critical solution temperature compound having a cloud point of 0 to 100° C.; and
removing at least partially the organic diluent and to the extent present in the medium removing at least partially the residual monomers to obtain an aqueous slurry comprising copolymer particles.

2. The process according to claim 1 , wherein the lower critical solution temperature compounds comprise lower critical solution temperature compounds having a cloud point of 0 to 100° C. determined by at least one of the following methods:
DIN EN 1890 of September 2006, method A;
DIN EN 1890 of September 2006, method C;
DIN EN 1890 of September 2006, method E;
DIN EN 1890 of September 2006, method A wherein the amount of compound tested is reduced from 1 g per 100 ml of distilled water to 0.05 g per 100 ml of distilled water; and
DIN EN 1890 of September 2006, method A wherein the amount of compound tested is reduced from 1 g per 100 ml of distilled water to 0.2 g per 100 ml of distilled water.

3. The process according to claim 1 or 2 , wherein the aqueous medium contains 20,000 ppm or less of further compounds which are not lower critical solution temperature compounds, whereby the further compounds are
selected from the group consisting of ionic or non-ionic surfactants, emulsifiers, and antiagglomerants, or are in another embodiment;
salts of (mono- or multivalent) metal ions, or are in another embodiment;
carboxylic acid salts of multivalent metal ions, or are in another embodiment;
stearates or palmitates of mono- or multivalent metal ions, or are in another embodiment; or
calcium and zinc stearates or palmitates.

4. The process according to claim 1 , wherein the aqueous medium comprises 1 to 2,000 ppm of antioxidants with respect to the amount of copolymer present in the copolymer medium.

5. The process according to claim 1 , wherein the at least one isoolefin is selected from the group consisting of isoolefin monomers having from 4 to 16 carbon atoms.

6. The process according to claim 1 , wherein the isoolefin is isobutene.

7. The process according to claim 1 , wherein the at least one multiolefin is selected from the group consisting of isoprene, butadiene, 2-methylbutadiene, 2,4-dimethylbutadiene, piperyline, 3-methyl-1,3-pentadiene, 2,4-hexadiene, 2-neopentylbutadiene, 2-methyl-1,5-hexadiene, 2,5-dimethyl-2,4-hexadiene, 2-methyl-1,4-pentadiene, 4-butyl-1,3-pentadiene, 2,3-dimethyl-1,3-pentadiene, 2,3-dibutyl-1,3-pentadiene, 2-ethyl-1,3-pentadiene, 2-ethyl-1,3-butadiene, 2-methyl-1,6-heptadiene, cyclopentadiene, methylcyclopentadiene, cyclohexadiene, and 1-vinyl-cyclohexadiene.

8. The process according to claim 1 , wherein the polymerization comprises slurry polymerization or solution polymerization.

9. The process according to claim 1 , wherein the contacting of the monomers with the initiator system, and the contacting of the copolymer medium with the aqueous medium, are independently carried out batchwise or continuously.

10. The process according to claim 1 , wherein the at least one lower critical solution temperature compound is selected from the group consisting of: poly(N-isopropylacrylamide), poly(N-isopropylacrylamide-co-N,N-dimethylacrylamide, poly(N-isopropylacrylamide)-alt-2-hydroxyethylmethacrylate, poly(N-vinylcaprolactam), poly(N,N-diethylacrylamide), poly[2-(dimethylamino)ethyl methacrylate], poly(2-oxazoline) glycopolymers, poly(3-ethyl-N-vinyl-2-pyrrolidone), hydroxylbutyl chitosan, polyoxyethylene (20) sorbitan monostearate, polyoxyethylene (20) sorbitan monolaurate, polyoxyethylene (20) sorbitan monooleate, methyl cellulose, hydroxypropyl cellulose, hydroxyethyl cellulose, hydroxyethyl methylcellulose, hydroxypropyl methylcellulose, poly(ethylene glycol) methacrylates with 2 to 6 ethylene glycol units, polyethyleneglycol-co-polypropylene glycols, compounds of formula (I)
HO—[—CH 2 —CH 2 —O] x —[—CH(CH 3 )—CH 2 —O] y —[—CH 2 —CH 2 —O] z —H  (I)

with y=3 to 10 and x and z=1 to 8, whereby y+x+z is from 5 to 18, polyethyleneglycol-co-polypropylene glycol, ethoxylated iso-C 13 H 27 -alcohols, polyethylene glycol with 4 to 50 ethyleneglycol units, polypropylene glycol with 4 to 30 propyleneglycol units, polyethylene glycol monomethyl, dimethyl, monoethyl and diethyl ether with 4 to 50 ethyleneglycol units, and polypropylene glycol monomethyl, dimethyl, monoethyl and diethyl ether with 4 to 50 propyleneglycol units.

11. The process according to claim 1 , wherein the amount of the lower critical solution temperature compound(s) present in the aqueous medium is 1 to 20,000 ppm with respect to the amount of copolymer present in the copolymer medium.

12. The process according to claim 1 , further comprising separating the copolymer particles contained in the aqueous slurry to obtain isolated copolymer particles.

13. The process according to claim 1 , further comprising separating the copolymer particles contained in the aqueous slurry to obtain isolated copolymer particles, and drying the copolymer particles.

14. The process according to claim 1 , further comprising shaping of the copolymer particles to obtain reshaped copolymer particles.

15. An aqueous slurry obtained by the process according to claim 1 .

Assignees

• Arlanxeo Singapore Pte Ltd

Inventors

• Thompson David
• Lund Clinton

Classifications

• C09K3/1006

  characterised by the chemical nature of one of its constituents · CPC title

• C08L23/22 Primary

  Copolymers of isobutene; Butyl rubber; Homopolymers or copolymers of other iso-olefins · CPC title

• C08K5/00

  Use of organic ingredients · CPC title

• C08J3/124

  Treatment for improving the free-flowing characteristics · CPC title

• C08J3/07 Primary

  from polymer solutions · CPC title