IP Library Granted Patent US 7,309,796
Granted Patent B2
US 7,309,796 · App. 11/050,382 · Granted Dec 18, 2007

Process for the preparation of 1,2-diaminocyclohexane-platinum(II) complexes

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Quick Facts
Patent No.
US 7,309,796
App. No.
11/050,382
Granted
Dec 18, 2007
Kind
B2
Abstract

A process for the preparation of diaminocyclohexane-platinum(II)-dicarboxylates has the following steps: B Conversion of K 2 PtX 2 with 1,2-diaminocyclohexane (DACH) to (2): C Conversion of (2) with too little quantity of silver salt Ag n A to (3): and removal of the resulting AgX precipitate. D Conversion of (3) with a dicarboxylate to (1): F Isolation of the product (1), wherein R 1 and R 2 together form a dicarboxylato group, X stands for Cl or I, A for a 1-2-valent anion of a mineral acid, and n stands for 1 or 2.

Claims (21)

1. A process for the preparation of diaminocyclohexane-platinum(II)-dicarboxylates comprising the following steps:

B) Converting K 2 PtX 4 with 1,2-diaminocyclohexane (DACH) to (2):

C) Converting (2) with a silver salt Ag n A to (3):

and removal of the resulting AgX precipitate;

D) Converting (3) with ammonium oxalate to (1):

F) Isolating the product (1),

wherein R 1 and R 2 together form a dicarboxylato group, X stands for CI or I, A stands for a 1-2-valent anion of a mineral acid, and n stands for 1 or 2, and wherein in step C an understochiometric amount of silver salt is used.

2. Process in accordance with claim 1 , wherein X is I.

3. Process in accordance with claim 2 , which is for the preparation of oxalipiatinum, and further comprises the following preceding step:

A) Converting K 2 PtCl 4 with Kl to K 2 Ptl 4 .

4. Process in accordance with claim 1 , wherein in step C the mixture is cooled to 1-10 degrees C. before the removal of the precipitate.

5. Process in accordance with claim 1 , wherein the solution derived after step D

E) is purified twice and filtered with activated carbon.

6. Process in accordance with claim 1 , wherein the solution derived after step D or E is concentrated to less than 10 ml/g product.

7. Process in accordance with claim 1 , which is conducted in purified endotoxin-free water with limited bacterial content (“purified water” according to European Pharmacopoeia, 4 th Edition, and/or U.S. Pharmacopoeia, 27 th Edition).

8. Process in accordance with claim 7 , whereby the water is “highly purified water” according to EP (European Pharmacopoeia, 4 th edition, 2002).

9. Process in accordance with claim 5 , wherein the solution derived after step E) is sterilely filtered and then concentrated and

F) the solid content is filtered and dried.

10. Process in accordance with claim 1 , wherein after step (F)

G) the product is washed with “purified water” according to European Pharmacopoeia, 4 th Edition, and/or U.S. Pharmacopoeia, 27 th Edition; or “highly purified water” according to European Pharmacopoeia, 4 th Edition; and subsequently washed with a light boiling solvent that is pharmacologically acceptable.

11. Process in accordance with claim 10 , wherein the solvent is acetone or methanol.

Assignments (2)
CHANGE OF NAME Recorded Nov 6, 2015
From: HERAEUS PRECIOUS METALS GMBH & CO. KG
To: HERAEUS DEUTSCHLAND GMBH & CO. KG
Reel/Frame 037056/0430 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 21, 2014
From: W.C. HERAEUS GMBH & CO. KG
To: HERAEUS PRECIOUS METALS GMBH & CO. KG
Reel/Frame 032973/0477 →