IP Library Granted Patent US 7,678,906
Granted Patent B2
US 7,678,906 · App. 12/027,432 · Granted Mar 16, 2010

Process for making triphenylboron-pyridine compound

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Quick Facts
Patent No.
US 7,678,906
App. No.
12/027,432
Granted
Mar 16, 2010
Kind
B2
Abstract

A process for improving the recovery of solid triphenylboron-pyridine compound (TPBP), while retaining desirable particle characteristics comprises the addition of an acid to neutralize at least a portion of the alkali contained in the aqueous mother liquor. By adjusting the pH of the product slurry to between about 8.5 and about 12, it is possible to increase product recovery by more than 10%, while maintaining desirable particle characteristics.

Claims (28)

1. A process for producing triphenylboron-pyridine (TPBP) comprising generally spherical solid particles which comprises:

(A) providing a product slurry comprising solid TPBP particles in an aqueous mother liquor in a vigorously agitated reaction zone;

(B) separately feeding into said vigorously agitated reaction zone (i) a stream of pyridine and (ii) a stream comprising a solution of an alkali hydroxide adduct of triphenylboron (TPBA), whereby the total concentration of TPBA in the combined feed streams is in the range of from about 1 wt % to about 6 wt %, to form additional TPBP in the product slurry;

(C) adding to the product slurry a sufficient amount of acid to adjust pH of the product slurry to a value of about 8.5 to about 12.0; and

(D) removing a product stream from said reaction zone at such a rate that the volume of said product slurry in the reaction zone remains substantially constant, and the concentration of solid TPBP in the product slurry is maintained at a value of less than about 8 wt %.

2. The process of claim 1 , wherein the amount of the acid added is sufficient to adjust the pH of the product slurry to a value of about 9 to about 12.

3. The process of claim 1 , wherein the amount of the acid added is sufficient to adjust the pH of the product slurry to a value of about 9.5 to about 11.

4. The process of claim 1 , wherein the amount of the acid added is sufficient to adjust the pH of the product slurry to a value of about 9.5 to about 10.5.

5. The process of claim 1 , wherein the acid is a non-oxidizing acid.

6. The process of claim 1 , wherein the acid is hydrochloric acid, sulfuric acid, phosphoric acid, or acetic acid.

7. The process of claim 1 , wherein the acid is hydrochloric acid.

8. The process of claim 1 , wherein the total concentration of TPBA in the combined feed streams is in the range of from about 3 wt % to about 5 wt %.

9. The process of claim 1 in which the temperature of the product slurry of solid TPBP particles in the aqueous mother liquor in the reaction zone is maintained in the range of from about 20° C. to about 60° C.

10. The process of claim 9 in which the temperature is maintained in the range of from about 35° C. to about 45° C.

11. A process for producing triphenylboron-pyridine (TPBP) which comprises:

(A) separately feeding into a reaction zone (i) a stream comprising pyridine and (ii) a stream comprising a solution of an alkali hydroxide adduct of triphenylboron (TPBA) to form a product slurry comprising TPBP in an aqueous mother liquor;

(B) adding to the reaction zone a sufficient amount of acid to adjust pH of the product slurry to a value of about 8.5 to about 12.0;

(C) removing a product stream from said reaction zone which includes the TPBP particles.

12. The process of claim 11 , wherein the amount of the acid added is sufficient to adjust the pH of the product slurry to a value of about 9 to about 12.

13. The process of claim 11 , wherein the amount of the acid added is sufficient to adjust the pH of the product slurry to a value of about 9.5 to about 11.

14. The process of claim 11 , wherein the amount of the acid added is sufficient to adjust the pH of the product slurry to a value of about 9.5 to about 10.5.

15. The process of claim 11 , wherein the acid is a non-oxidizing acid.

16. The process of claim 11 , wherein the acid is hydrochloric acid, sulfuric acid, phosphoric acid, or acetic acid.

17. The process of claim 11 , wherein the acid is hydrochloric acid.

18. A process of claim 1 , wherein the acid is added to the reaction zone.

19. A process of claim 1 , wherein the acid is added in a vessel separate from the reaction zone.

20. A process of claim 11 , wherein the acid is added to the reaction zone.

21. A process of claim 11 , wherein the acid is added to a vessel separate from the reaction zone.

Assignments (5)
RELEASE OF SECURITY INTEREST Recorded Nov 10, 2011
From: DEUTSCHE BANK AG NEW YORK BRANCH
To: INVISTA NORTH AMERICA S.A.R.L.
Reel/Frame 027211/0298 →
SECURITY AGREEMENT Recorded Mar 19, 2009
From: INVISTA NORTH AMERICA S.A.R.L.
To: DEUTSCHE BANK AG NEW YORK BRANCH, AS COLLATERAL AGENT
Reel/Frame 022416/0849 →
RELEASE OF U.S. PATENT SECURITY INTEREST Recorded Mar 19, 2009
From: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT AND COLLATERAL AGENT (F/K/A JPMORGAN CHASE BANK)
To: INVISTA NORTH AMERICA S.A.R.L. (F/K/A ARTEVA NORTH AMERICA S.A.R.L.)
Reel/Frame 022427/0001 →
SECURITY AGREEMENT Recorded Jul 7, 2008
From: INVISTA NORTH AMERICA, S.A.R.L.
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 021199/0782 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 10, 2008
From: OSTERMALER, JOHN J.
To: INVISTA NORTH AMERICA S.A.R.L.
Reel/Frame 020626/0697 →