Process for the production of expanded materials based on polyurea elastomers

• US 5,189,073 A
• Filed: 03/19/1992
• Issued: 02/23/1993
• Est. Priority Date: 03/19/1991
• Status: Expired due to Term

• Current Assignee: Huntsman Petrochemical LLC (Huntsman Corporation)
• Original Assignee: Texaco Chemical Company (Huntsman Corporation)
• Inventors: Humbert, Heiko, Primeaux, Dudley J. II, Klockemann, Werner
• Primary Examiner(s): WELSH JR, MAURICE
• Application Number:
  US07/855,357
• Time in Patent Office: 341 Days
• Field of Search: 521/110, 521/129, 521/133, 521/159, 521/163, 528/48, 528/53, 528/60, 528/61, 528/68
• US Class Current: 521/110
• CPC Class Codes: C08G 18/0895 Manufacture of polymers by continuous processes C08G18/0838 takes precedence
• CPC Class Codes: C08G 18/18 containing secondary or tertiary amines or salts thereof
• CPC Class Codes: C08G 18/1825 having hydroxy or primary amino groups
• CPC Class Codes: C08G 18/20 Heterocyclic amines; Salts thereof
• CPC Class Codes: C08G 18/3265 with carbondioxide or sulfurdioxide
• CPC Class Codes: C08G 18/503 being in latent form
• CPC Class Codes: C08G 2110/005 < 50kg/m3
• CPC Class Codes: C08G 2110/0058 ≥50 and <150kg/m3
• CPC Class Codes: C08J 2375/04 Polyurethanes
• CPC Class Codes: C08J 9/122 Hydrogen, oxygen, CO2, nitrogen or noble gases

Abstract

A process for the production of expanded polyurea elastomers which comprises reacting:

a) an aliphatic polyetheramine having primary amino functions and essentially no free hydroxyl groups;

b) carbon dioxide in the form of carbamate, obtained by reacting carbon dioxide with a portion of the aliphatic polyetheramines;

c) a polyisocyanate;

d) water; and

e) a catalyst having a tertiary amino group;

in the presence of

f) an inert, halogen-free blowing agent.

Claims

1. A process for the production of expanded polyurea elastomers comprising reacting:

a) an aliphatic polyetheramine having primary amino functions and essentially no free hydroxyl groups;

b) carbon dioxide in the form of carbamate, obtained by reacting carbon dioxide with a portion of the aliphatic polyetheramines;

c) a polyisocyanate;

d) water; and

e) a catalyst having a tertiary amino group;

in the presence of

f) an inert, halogen-free blowing agent.

2. The process according to claim 1 wherein the aliphatic polyetheramine comprises compounds of general formula

3. The process according to claim 1 wherein the aliphatic polyetheramine comprises compounds of general formula:

space="preserve" listing-type="equation">R.sup.2 [[O(CH.sub.2).sub.m CHR.sup.1 ].sub.n (OCH.sub.2 CH.sub.2 CH.sub.2).sub.o NH.sub.2 ].sub.3

where

n denotes an integer between about 1 and about 100;

o denotes 0 or 1;

R¹ denotes hydrogen and m denotes the number 1 or 3, or

R¹ denotes methyl and m denotes the number 1; and

R² denotes a trivalent radical chosen from the group consisting of;

CH₃ --C(CH₂ --)₃, CH₃ --CH₂ --C(CH₂ --)₃, and (--CH₂)₂ CH--.

4. The process according to claim 2 wherein R¹ is methyl and m is 1.

5. The process according to claim 3 wherein R¹ is methyl and m is 1.

6. The process according to claim 2 wherein the polyetheramines have an Mn of about 200 to about 12,000.

7. The process according to claim 3 wherein the polyetheramines have an Mn of about 200 to about 12,000.

8. The process according to claim 1 wherein the polyisocyanate comprises diphenylmethane diisocyanate.

9. The process according to claim 1 wherein the polyisocyanate comprises diphenylmethane diisocyanate and toluylidene diisocyanate.

10. The process according to claim 1 wherein the polyisocyanate includes prepolymers thereof.

11. The process according to claim 1 wherein the polyetheramine and the polyisocyanate are used in relative amounts corresponding to a molar ratio of NH₂ to NCO groups in the range of 1:

1.5 to 1;

7.

12. The process according to claim 1 wherein 1 to 4 moles of water are employed per mole of NCO groups which are present in excess, based on NH₂ groups.

13. The process according to claim 1 wherein the catalyst having a tertiary amino group comprises a compound of general formula:

space="preserve" listing-type="equation">XCH.sub.2 CH.sub.2 MCH.sub.2 CH.sub.2 Y

where

M denotes oxygen or a methylimino group;

X is chosen from the group consisting of N-morpholinyl, N-azanorbornyl, dimethylamino and dimethylaminoethyl groups; and

Y is chosen from the group consisting of N-morpholinyl, N-azanorbornyl, dimethylamino, dimethylaminoethyl, hydroxyl and N-methyl-N-(2-hydroxy-C₁ -C₂ -alkyl)-amino group.

14. The process according to claim 1 wherein the catalyst having a tertiary amino group is chosen from the group consisting of 2,2-dimorpholinodiethyl ether, 2-(2-dimethylamino)-ethoxyethanol, bis-(2-dimethylaminoethyl) ether, 2-(2 dimethyl-aminoethyl)-2-methylaminoethanol and 2-(2-dimethylaminoethoxy)-ethylmethylaminoethanol.

15. The process according to claim 1 wherein the catalyst having a tertiary amino group is 2,2,4-trimethyl-1-oxa-2-sila-4-azacyclohexane.

16. The process according to claim 1 wherein the catalyst having a tertiary amino group is employed in amounts ranging from about 0.01 to about 5 phr based on the polyetheramines.

17. The process according to claim 1 wherein the catalyst having a tertiary amino group is employed in amounts ranging from about 0.05 to about 3 phr based on the polyetheramines.

18. The process according to claim 1 wherein the inert, halogen-free blowing agent is a material selected from the group consisting of carbon dioxide, nitrogen and dry air.

19. The process according to claim 1 wherein separate streams comprising

a) the aliphatic polyetheramine, the catalyst having a tertiary amino group, the carbon dioxide in the form of carbamate, and the dissolved inert, halogen-free blowing agent.;

b) the polyisocyanate; and

c) water

are fed to a mixing head, and the mixture obtained is allowed to react to completion after leaving the mixing head.

20. The process according to claim 19 wherein the stream comprising the aliphatic polyetheramine, the catalyst having a tertiary amino group, the carbon dioxide bound as carbamate and the dissolved inert, halogen-free blowing agent further comprises a polyurea additive.

21. The process according to claim 1 wherein the reaction is carried out at superatmospheric pressure.