Use of polyurea nanoparticles as performance modifiers in polyurethane materials

Patent metadata

Field	Value
Publication number	US-9926424-B2
Application number	US-201314413238-A
Country	US
Kind code	B2
Filing date	Jun 28, 2013
Priority date	Jul 17, 2012
Publication date	Mar 27, 2018
Grant date	Mar 27, 2018

Abstract

Nano-sized polyurea particles or a dispersion of polyurea particles suitable for improving the mechanical properties of a polyurethane material, said particles having at least equivalent diameter dimensions in the nanosize range of 50 nm up to 700 nm, a uniform equivalent diameter particle size distribution, an amount of urethane bonds calculated on the total amount of urea+urethane bonds in said particles of <1%, and a glass transition temperature (Tg) of >100° C., preferably Tg>120° C., more preferably >150° C. measured in a second heating cycle after heating to >220° C. at 20° per minute using Differential Scanning calorimetry.

First claim

The invention claimed is:

1. A method for making nano-sized polyurea particles or a dispersion of said polyurea particles having an equivalent diameter in the range of 50 nm up to 700 nm, a narrow equivalent diameter particle size distribution wherein the relative span d 90 −d 10 /d 50 <3, a ratio of urea bonds to urethane bonds in said particles of at least 90:10, and a glass transition temperature (Tg) of >100° C., measured in a second heating cycle after heating to >220° C. at 20° per minute using Differential Scanning Calorimetry, said method comprising the steps of
combining an isocyanate-reactive monoamine component with a polyisocyanate component thereby forming an urea-modified polyisocyanate component optionally dissolved in a solvent, and then
adding said urea-modified polyisocyanate component to a diamine component thereby forming polyurea particles optionally dispersed in a solvent
characterized in that the diamine component is selected from components corresponding to structure [2]:
H 2 N—(A 5 ) q —NH 2   [2]

Wherein
q is an integer smaller than 4,
A 5 may be a C2, C3 or branched C3 group,
A 5 may be one or more aromatic group,
A 5 may be an aryl-aliphatic wherein the aliphatic part is a C1 up to C6 and further comprises 1-4 aromatic groups,
A 5 may be cyclo-aliphatic group of C3 up to C15 and
A 5 may further comprise an ether group and/or one or more NH groups.

2. The method according to claim 1 , wherein the diamine component is selected from ethylenediamine, tricyclodecanediamine, hexamethylenediamine, neopentanediamine, diethyltoluenediamine, 4-methyl-1,2-phenylenediamine.

3. The method according to claim 1 , wherein the monoamine components are alkylpolyoxyalkyl monoamines represented by following general structure [1]:
A 1 —(OA 2 ) n —(OA 3 ) m —(OA 4 ) p —NH 2   [1]

wherein
A 1 is a C1 to C6 chain,
A 2 , A 3 and A 4 are mutually different C1 to C6 chains, and

n, m and p independently are a positive integers.

4. The method according to claim 1 , wherein the monoamine components are alkylpolyoxyalkyl monoamines represented by following general structure [1]:
A 1 —(OA 2 ) n —(OA 3 ) m —(OA 4 ) p —NH 2   [1]

wherein A 1 is C 9 H 19 -Ø-, wherein Ø is an aromatic C6-ring.

5. The method according to claim 1 , wherein the ratio of isocyanate groups in the polyisocyanate component calculated over the total number of reactive hydrogens in the monoamine component and diamine component is in the range of 80 up to 120.

6. The method according to claim 1 , wherein the ratio of isocyanate groups in the polyisocyanate component over the number of primary and secondary amine groups in the monoamine component is in the range of 1.6 up to 120.

7. The method according to claim 1 , wherein suitable solvents include ketones such as acetone, tetrahydrofuran (THF), toluene, and polyols which are reactive towards isocyanates at temperatures above 60° C.

8. The method according to claim 1 , wherein the dispersion of polyurea particles has 0.5 wt % up to 50 wt % of particles in a suitable solvent.

9. The method according to claim 1 , wherein the relative span d 90 −d 10 /d 50 is <2.5.

10. The method according to claim 1 , wherein the glass transition temperature (T g ) is >120° C.

11. The method according to claim 1 , wherein the glass transition temperature (T g ) is >150° C.

12. The method according to claim 1 , wherein the ratio of urea bonds to urethane bonds is 99:1.

13. The method according to claim 5 , wherein the ratio of isocyanate groups in the polyisocyanate component calculated over the total number of reactive hydrogens in the monoamine component and diamine component ranges from 90 up to 110.

14. The method according to claim 5 , wherein the ratio of isocyanate groups in the polyisocyanate component calculated over the total number of reactive hydrogens in the monoamine component and diamine component ranges from 99 up to 101.

15. The method according to claim 6 , wherein the ratio of isocyanate groups in the polyisocyanate component calculated over the total number of reactive hydrogens in the monoamine component and diamine component ranges from 10 up to 70.

16. The method according to claim 6 , wherein the ratio of isocyanate groups in the polyisocyanate component calculated over the total number of reactive hydrogens in the monoamine component and diamine component ranges from 20 up to 40.

17. The method according to claim 8 , wherein the dispersion of polyurea particles has 1 wt % up to 30 wt % of particles in a suitable solvent.

18. The method according to claim 8 , wherein the dispersion of polyurea particles has 5 wt % to 20 wt % of particles in a solvent.

Assignees

• Huntsman Int Llc

Inventors

• Woutters Steve Andre
• Lindsay Christopher Ian

Classifications

• C08J2375/08

  from polyethers · CPC title

• C08G18/3234

  cycloaliphatic · CPC title

• C08G18/3206

  aliphatic · CPC title

• C08J9/125 Primary

  Water, e.g. hydrated salts · CPC title

• C08G18/7671 Primary

  containing only one alkylene bisphenyl group · CPC title