Biocide- and ammonia-free polymer dispersions

Patent metadata

Field	Value
Publication number	US-11608441-B2
Application number	US-201716766614-A
Country	US
Kind code	B2
Filing date	Nov 29, 2017
Priority date	Nov 29, 2017
Publication date	Mar 21, 2023
Grant date	Mar 21, 2023

Abstract

A biocide- and ammonia-free aqueous polymer dispersion is obtained by radically initiated multi-stage emulsion polymerization and comprising particles comprising at least a first polymer phase formed from a monomer composition I and a second polymer phase from a different monomer composition II. The first polymer phase has a glass transition temperature below 20° C., and the second polymer phase has a glass transition temperature above 20° C., both as determined by differential scanning calorimetry according to ISO 16805. The polymer dispersion further comprises at least one water-soluble alkali metal silicate, at least one water-soluble alkali metal or alkaline earth metal alkyl siliconate, or a mixture thereof and has a pH of 10.0 or higher.

First claim

What is claimed is:

1. A biocide- and ammonia-free aqueous polymer dispersion obtained by radically initiated multi-stage emulsion polymerization and comprising particles comprising at least a first polymer phase formed from a monomer composition I and a second polymer phase from a different monomer composition II,
wherein the first polymer phase has a glass transition temperature below 20° C., and wherein the second polymer phase has a glass transition temperature above 20° C., both as determined by differential scanning calorimetry according to ISO 16805,
wherein the polymer dispersion further comprises at least one water-soluble alkali metal silicate, at least one water-soluble alkali metal alkyl siliconate, at least one water-soluble alkaline earth metal alkyl siliconate, or a mixture thereof,
and wherein the pH of the polymer dispersion is 10.0 or higher.

2. An aqueous polymer dispersion according to claim 1 , wherein the first polymer phase has a glass transition temperature in the range of from −30 to 10° C., and wherein the second polymer phase has a glass transition temperature above 30° C., both as determined by differential scanning calorimetry according to ISO 16805.

3. An aqueous polymer dispersion according to claim 1 , wherein at least one of monomer compositions I or II comprises monomers selected from the group consisting of esters of acrylic or methacrylic acid, styrene and mixtures thereof.

4. An aqueous polymer dispersion according to claim 1 , wherein monomer compositions I and II comprise at least 50% of monomers selected from the group consisting of esters of acrylic or methacrylic acid, styrene and mixtures thereof.

5. An aqueous polymer dispersion according to claim 1 , wherein at least one of monomer compositions I or II comprises monomers selected from the group of ethylenically unsaturated sulfonic acids, ethylenically unsaturated phosphonic and phosphoric acids, ethylenically unsaturated carboxylic acids, ethylenically unsaturated carboxylic amides, ethylenically unsaturated carboxylic anhydrides and mixtures thereof.

6. An aqueous polymer dispersion according to claim 1 , wherein at least one of monomer compositions I or II comprise monomers selected from the group of ethylenically unsaturated sulfonic acids, ethylenically unsaturated carboxylic amides, and mixtures thereof.

7. An aqueous polymer dispersion according to claim 1 , wherein at least one of monomer compositions I or II comprise a mixture of at least one ethylenically unsaturated sulfonic acid and at least one ethylenically unsaturated carboxylic amide.

8. An aqueous polymer dispersion according to claim 1 , wherein the pH of the polymer dispersion is in the range of 10.0 to 12.0.

9. An aqueous polymer dispersion according to claim 1 having a minimum film forming temperature (MFFT) less than 6° C.

10. An aqueous polymer dispersion according to claim 1 having a Total Volatile Organic Compound (TVOC) content less than 2000 ppm, as determined by gas chromatography according to ISO 11890-2.

11. An aqueous polymer dispersion according to claim 1 , wherein the polymer particles have a weight-averaged diameter of less than 150 nm, as measured by a combination of laser diffraction and polarization intensity differential scattering (PIDS) using a Beckman Coulter LS 13320 Particle Size Analyzer.

12. An aqueous polymer dispersion according to claim 1 , wherein the polymer dispersion comprises, based on the total weight of the polymer dispersion, 0.1 to 4 wt. % of at least one water-soluble alkali metal silicate, at least one water-soluble alkali metal alkyl siliconate, at least one water-soluble alkaline earth metal alkyl siliconate, or a mixture thereof.

13. An aqueous polymer dispersion according to claim 1 , wherein the polymer dispersion comprises 0.1 to 4 wt. % potassium silicate, potassium methyl siliconate, or a mixture thereof.

14. An aqueous polymer dispersion according to claim 1 , wherein the polymer dispersion comprises 0.1 to 4 wt. % potassium silicate.

15. An aqueous polymer dispersion according to claim 1 and exhibiting a pH drop less than 1.0, when stored for 28 days at 50° C.

16. A process for preparing an aqueous polymer dispersion according to claim 1 by multi-stage emulsion polymerization, wherein each of the monomer compositions I and II is emulsified and polymerized in aqueous phase in the presence of emulsifiers, initiators and optionally protective colloids at a polymerization temperature ranging from 50 to 95° C.

17. A process according to claim 16 , wherein the monomer composition I is polymerized in a first stage to obtain the first polymer phase, and subsequently the monomer composition II is polymerized in a second stage to obtain the second polymer phase.

18. A process according to claim 16 , wherein at least one water-soluble alkali metal silicate, at least one water-soluble alkali metal or alkaline earth metal alkyl siliconate, or a mixture thereof is post-added to the dispersion below 50° C.

19. A process according to claim 16 , wherein part of either monomer composition I or II is prepolymerized before the remaining parts of monomer compositions I and II are supplied to the multi-stage emulsion polymerization.

20. A coating composition comprising the aqueous polymer dispersion according to claim 1 .

21. A coating composition according to claim 20 having more than 10 gloss units, when measured with a glossmeter at an angle of 85° according to ASTM D523.

22. A coating composition according to claim 20 , which fulfills the requirements of the EU Ecolabel as defined in the Commission Decision 2014/312/EU regarding Total Volatile Organic Compound (TVOC) and Total Semi Volatile Organic Compound (TsVOC) content.

23. A coating composition according to claim 20 having a TVOC content less than 1000 ppm, as determined by gas chromatography according to ISO 11890-2.

24. A coating composition according to claim 20 , which is free of any organic solvent, plasticizer or coalescent agent.

25. A coating composition according to claim 20 , having at least a wet scrub class II according to EN 13300.

Assignees

• Celanese Int Corp

Inventors

• Junk Matthias
• Fichtner Thomas

Classifications

• C08F2/001

  Multistage polymerisation processes characterised by a change in reactor conditions without deactivating the intermediate polymer (C08F295/00, C08F297/00 take precedence) · CPC title

• C08F220/1804

  C4-(meth)acrylate, e.g. butyl (meth)acrylate, isobutyl (meth)acrylate or tert-butyl (meth)acrylate · CPC title

• C08L33/08

  Homopolymers or copolymers of acrylic acid esters · CPC title

• C08F2/24

  with the aid of emulsifying agents · CPC title

• C09D133/08

  Homopolymers or copolymers of acrylic acid esters · CPC title