Method for producing water-soluble homopolymers or copolymers which comprise (meth)acrylamide

Patent metadata

Field	Value
Publication number	US-10233272-B2
Application number	US-201515303695-A
Country	US
Kind code	B2
Filing date	Apr 10, 2015
Priority date	Apr 15, 2014
Publication date	Mar 19, 2019
Grant date	Mar 19, 2019

Abstract

A process for preparing water-soluble homo- or copolymers comprising (meth)acrylamide by free-radical polymerization of an aqueous solution of monoethylenically unsaturated monomers comprising at least (meth)acrylamide in the presence of at least one stabilizer for prevention of polymer degradation by molecular oxygen. The stabilizer is preferably one selected from the group of sulfur compounds, sterically hindered amines, N-oxides, nitroso compounds, aromatic hydroxyl compounds and ketones, more preferably 2-mercaptobenzothiazole or a salt thereof.

First claim

The invention claimed is:

1. A process for preparing water-soluble homopolymers or copolymers comprising (meth)acrylamide by free-radical polymerization of an aqueous solution of ethylenically unsaturated monomers comprising at least (meth)acrylamide in the presence of at least one stabilizer, wherein the polymerization is a gel polymerization, and the process comprises at least the following steps:
(I) providing an aqueous monomer solution comprising
water,
25 to 45% by weight based on the amount of all the components of the aqueous solution of ethylenically unsaturated monomers (A), where at least 70% by weight of the monomers are monoethylenically unsaturated, hydrophilic monomers (A1), with the proviso that at least one of the monomers (A1) is (meth)acrylamide,
0.1 to 2% by weight —based on the sum total of all the monomers —of at least one stabilizer (B) for prevention of polymer degradation by molecular oxygen, the at least one stabilizer selected from the group of sulfur compounds, sterically hindered amines, N-oxides, nitroso compounds, aromatic hydroxyl compounds and ketones,
an azo initiator (C) having a 10 h half-life of 40° C. to 75° C., where the aqueous monomer solution
has a pH of <7,
is at a temperature of <5° C., and
has been inertized,

(II) adding at least one redox initiator (D) to the aqueous monomer solution at a temperature of less than 5° C.,
(III) polymerizing the aqueous monomer solution under essentially adiabatic conditions, the initiation temperature of the polymerization being less than 5° C., to provide a reaction mixture that is heated with the heat of polymerization to a temperature of 60° C. to 100° C., to provide a polymer gel, and
(IV) drying the polymer gel.

2. The process according to claim 1 , wherein the at least one stabilizer (B) is selected from the group of thiourea, N,N′-dimethylthiourea, N,N′-diethylthiourea, N,N′-diphenylthiourea, thiocyanates, tetramethylthiuram disulfide, 2-mercaptobenzothiazole or salts thereof, 2-mercaptobenzimidazole or salts thereof, sodium dimethyldithiocarbamate, 2,2′-dithiobis(benzothiazole), 4,4′-thiobis(6-t-butyl-m-cresol), dicyandiamide, guanindine, cyanamide, paramethoxyphenol, 2,6-di-t-butyl-4-methylphenol, butylhydroxyanisole, 8-hydroxyquinoline, 2,5-di(t-amyl)hydroquinone, 5-hydroxy-1,4-naphthoquinone, dimedone, propyl 3,4,5-trihydroxybenzoate, ammonium N-nitrosophenylhydroxylamine, 4-hydroxy-2,2,6,6-tetramethyoxylpiperidine, (N-(1,3-dimethylbutyl)-N′-phenyl-p-phenylenediamine and 1,2,2,6,6-pentamethyl-4-piperidinol.

3. The process according to claim 1 , wherein the stabilizer (B) is 2-mercaptobenzothiazole or a salt thereof.

4. The process according to claim 1 , wherein the initiation temperature of the polymerization is of −4° C. to +4° C.

5. The process according to claim 1 , wherein the reaction mixture is heated to a temperature of 80° C. to 100° C.

6. The process according to claim 1 , wherein the pH of step (I) is adjusted to 6 to 6.5.

7. The process according to claim 1 , wherein the concentration of the monomers is 30 to 40% by weight.

8. The process according to claim 1 , wherein the proportion of (meth)acrylamide is at least 30% by weight based on the sum total of all the monomers.

9. The process according to claim 1 , wherein the proportion of (meth)acrylamide is at least 50% by weight based on the sum total of all the monomers.

10. The process according to claim 1 , wherein the polymerization is conducted in a conical reactor.

11. The process according to claim 10 , wherein the conical reactor is a tubular reactor ( 1 ) which has a diameter D 1 and narrows conically ( 2 ) at the lower end, where the diameter at the end of the conical narrowing is D 2 , the ratio D 1 /D 2 is 2:1 to 25:1 and the angle α between the wall in the cylindrical section ( 1 ) and the wall in the region of the conical narrowing ( 2 ) is more than 120° and less than 180°, and the tubular reactor including a shut-off device ( 3 ) arranged at the lower end of the conical narrowing and at least one feed ( 4 ) at the upper end of the reactor, and
at least step (I) is undertaken in suitable mixing and cooling devices outside the conical reactor,
the cooled monomer solution is transferred from the suitable mixing and cooling devices to the feed ( 4 ) into the reactor, and
after the polymerization, the shut-off device ( 3 ) is opened, and injecting at least one gas through the feed ( 4 ), the polymer gel ( 5 ) is forced out of the reactor through the opened shut-off device.

12. The process according to claim 11 , wherein the adding of the solution of the redox initiator (D) is conducted during the feeding of the monomer solution through the feed ( 4 ).

13. A process for preparing water-soluble homopolymers or copolymers comprising (meth)acrylamide by free-radical polymerization of an aqueous solution of ethylenically unsaturated monomers comprising at least (meth)acrylamide in the presence of at least one stabilizer, wherein the polymerization is a gel polymerization and the process comprises at least the following steps:
(Ia) providing an aqueous monomer solution comprising at least
water,
25 to 45% by weight —based on the amount of all the components of the aqueous solution —of ethylenically unsaturated monomers (A), where at least 70% by weight of the monomers are monoethylenically unsaturated, hydrophilic monomers (A1), with the proviso that at least one of the monomers (A1) is (meth)acrylamide,
0.1 to 2% by weight —based on the sum total of all the monomers —of at least one stabilizer (B) for prevention of polymer degradation by molecular oxygen, the at least one stabilizer selected from the group of sulfur compounds, sterically hindered amines, N-oxides, nitroso compounds, aromatic hydroxyl compounds and ketones,
an azo initiator (C) having a 10 h half-life of 40° C. to 75° C.,
a photoinitiator (E),

where the aqueous monomer solution
has a pH of <7,
is at a temperature of <5° C. and
has been inertized,

(IIIa) polymerizing the aqueous monomer solution under essentially adiabatic conditions, the initiation temperature of the polymerization being less than 5° C. and the polymerization being triggered by irradiation of the monomer solution with UV radiation, to provide a reaction mixture that is heated with the heat of polymerization to a temperature of 60° C. to 100° C., to provide a polymer gel, and
(IV) drying the polymer gel.

14. The process according to claim 1 , wherein the at least one of the monomers (A1) is selected from sodium acrylate or sodium salt of 2-acrylamido-2-methylpropanesulfonic acid.

15. The process according to claim 14 , wherein the polymer gel has an MPFR value of 1.02 to 1.16.

16. The process according to claim 14 , wherein the polymer gel has an MPFR value of 1.02 to 1.09.

17. The process according to claim 1 , wherein the pH of step (I) is adjusted to 5 to 6.9.

18. The process according to claim 14 , wherein the pH of step (I) is adjusted to 5 to 6.9.

Assignees

• Basf Se

Inventors

• Langlotz Björn

Classifications

• C08J3/28

  Treatment by wave energy or particle radiation · CPC title

• C08F2/50

  with sensitising agents · CPC title

• C08F2/38

  Polymerisation using regulators, e.g. chain terminating agents {, e.g. telomerisation} · CPC title

• C08F2/01

  characterised by special features of the polymerisation apparatus used · CPC title

• C08F220/56 Primary

  Acrylamide; Methacrylamide · CPC title