IP Library Granted Patent US 10,711,018
Granted Patent B2
US 10,711,018 · App. 16/381,091 · Granted Jul 14, 2020

Process for preparing tris[3-(alkyldialkoxysilyl)propyl]isocyanurates

Inventors: Philipp Albert (Rheinfelden, DE); Eckhard Just (Rheinfelden, DE)
Assignee: Evonik Operations GmbH
C07F7/1876B01J31/2291
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,711,018
App. No.
16/381,091
Granted
Jul 14, 2020
Kind
B2
Abstract

A process can prepare an isocyanurate compound by hydrosilylation. The compound is a tris[3-(trialkoxysilyl)propyl] isocyanurate, a tris[3-(alkyldialkoxysilyl)propyl] isocyanurate, and/or a tris[3-(dialkylalkoxysilyl)propyl] isocyanurate, The process includes (A) preparing a mixture of at least one carboxylic acid, a platinum catalyst, and 1,3,5-triallyl-1,3,5-triazine-2,4,6(1H,3H,5H)-trione; (B) heating the mixture to a temperature in the range of 40 to 140° C.; (C) adding at least one H-silane among a hydrotrialkoxysilane, a hydroalkyldialkoxysilane, and a hydrodialkylalkoxysilane to the mixture; (D) adding at least one alcohol to the mixture prepared in step (C); and (E) isolating the isocyanurate compound.

Claims (24)

1. A process for preparing a tris[3-(alkyldialkoxysilyl)propyl]isocyanurate of the formula:

comprising the following steps:

(A) preparing a mixture comprising at least one carboxylic acid, a platinum catalyst and 1,3,5-triallyl-1,3,5-triazine-2,4,6(1H,3H,5H)-trione of the formula:

(B) heating the mixture prepared in step (A) to a temperature in the range of 40° C.-140° C.;

(C) adding a hydrosilane of the formula:

to the mixture prepared in step (B);

(D) adding at least one alcohol to the mixture prepared in step (C); and

(E) isolating the tris[3-(alkyldialkoxysilyl)propyl]isocyanurate of the formula above.

2. The process according to claim 1 , wherein the molar ratio of the hydrosilane to the at least one alcohol is 1:0.005-0.3.

3. The process according to claim 1 , wherein the molar ratio of the hydrosilane to the platinum catalyst is 1:0.000000001-0.0001.

4. The process according to claim 1 , wherein the molar ratio of the hydrosilane to the at least one carboxylic acid is 1:0.001-0.03.

5. The process according to claim 1 , wherein the molar ratio of the hydrosilane to 1,3,5-triallyl-1,3,5-triazine-2,4,6(1H,3H,5H)-trione is 1:0.1-1.

6. The process according to claim 1 , wherein the at least one carboxylic acid is selected from the group consisting of benzoic acid, propionic acid, 2,2-dimethylpropionic acid, 3,5-di-tert-butylbenzoic acid, 3,5-di-tert-butyl-4-hydroxybenzoic acid and acetic acid.

7. The process according to claim 1 , wherein the at least one alcohol is a C 1 -C 10 alcohol.

8. The process according to claim 1 , wherein the at least one alcohol is selected from the group consisting of methanol, ethanol, tert-butanol, benzyl alcohol and diglycol monomethyl ether.

9. The process according to claim 1 , wherein the at least one alcohol is ethanol.

10. The process according to claim 1 , wherein the platinum catalyst is selected from the group consisting of a Karstedt catalyst, a hexachloroplatinum(IV) acid and platinum adsorbed on a solid support.

11. The process according to claim 1 , wherein the platinum catalyst is selected from the group consisting of a platinum(0)-1,3-divinyl-1,1,3,3-tetramethyldisiloxane complex in the form of a Karstedt catalyst in xylene or toluene with a 0.5%-5% w/w platinum(0) content, hexachloroplatinum(IV) acid dissolved in acetone and platinum adsorbed on activated carbon.

12. The process according to claim 1 , wherein the platinum catalyst is a platinum(0)-1,3-divinyl-1,1,3,3-tetramethyldisiloxane complex in the form of a Karstedt catalyst in xylene or toluene with a 0.5%-5% w/w platinum(0) content.

13. The process according to claim 1 , wherein the process further comprises performing step (C) at a temperature in the range of 86° C.-120° C.

14. The process according to claim 1 , wherein the process further comprises performing step (D) at a temperature in the range of 96° C.-111° C.

15. The process according to claim 1 , wherein the process further comprises recovering the platinum catalyst from the mixture formed in step (D) prior to performing step (E).

16. The process according to claim 1 , wherein the process further comprises performing step (E) via distillation at a temperature in the range of 45° C.-150° C. and at a pressure less than 1 bar.

17. The process according to claim 1 , wherein at least 90 mol % of the allyl groups in the 1,3,5-triallyl-1,3,5-triazine-2,4,6(1H,3H,5H)-trione are converted by hydrosilylation to 3-(alkyldialkoxysilyl)propyl groups.

Assignments (1)
CHANGE OF NAME Recorded Nov 18, 2019
From: EVONIK DEGUSSA GMBH
To: EVONIK OPERATIONS GMBH
Reel/Frame 051045/0872 →
Priority Claims (1)
EP 17159900 · Mar 8, 2017 · regional
Continuity (3)
Continuation 16159763 · Oct 15, 2018
Continuation In Part 15915126 · Mar 8, 2018
Related Publication 20190233445A1 · Aug 1, 2019