IP Library Granted Patent US 7,423,183
Granted Patent B2
US 7,423,183 · App. 10/558,162 · Granted Sep 9, 2008

Oxidation of mercaptoethanol

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Quick Facts
Patent No.
US 7,423,183
App. No.
10/558,162
Granted
Sep 9, 2008
Kind
B2
Abstract

A process for preparing dihydroxyethylene disulfide by reacting mercaptoethanol with oxygen, in which mercaptoethanol is reacted with oxygen or an oxygenous gas in the presence of ammonia and/or amines using copper salts or manganese salts.

Claims (18)

1. A process for preparing dihydroxyethylene disulfide by reacting mercaptoethanol with oxygen, comprising the step of reacting mercaptoethanol with oxygen or an oxygenous gas in the presence of ammonia and/or amines using copper salts or manganese salts.

2. The process as claimed in claim 1 , wherein the copper salts used are copper(II) salts.

3. The process as claimed in claim 1 , wherein the manganese salts used are manganese (II) salts.

4. The process as claimed in claim 2 , wherein the copper (II) salt is copper acetate.

5. The process as claimed in claim 3 , wherein the manganese (II) salt is manganese acetate.

6. The process as claimed in claim 1 , wherein mercaptoethanol is initially charged and oxygen is metered into the initial charge.

7. The process as claimed in claim 1 , wherein the reaction is carried out under a partial oxygen pressure of from 0.5 to 5 bar.

8. The process as claimed in claim 4 , wherein the reaction is carried out under an elevated oxygen pressure of 1-5 bar.

9. The process as claimed in claim 8 characterized in that the reaction is carried out at a pressure of 1-2.5 bar.

10. The process as claimed in claim 4 , wherein the reaction is carried out under a constant oxygen pressure.

11. The process as claimed in claim 4 , wherein a stoichiometric amount of oxygen is used for the reaction.

12. The process as claimed in claim 4 , wherein aqueous ammonia is used.

13. The process as claimed in claim 4 , wherein the metal salt used is dissolved in ammonia or in the amine.

14. The process as claimed in claim 4 , wherein the reaction is carried out at from 20 to 60° C.

15. The process as claimed in claim 14 , characterized in that the reaction is carried out at from 35 to 45° C.

16. The process as claimed in claim 4 , wherein the reaction is carried out in the absence of organic solvents.

17. The process as claimed in claim 4 , wherein the reaction is carried out in an aqueous medium.

18. The process as claimed in claim 17 , wherein the reaction is used in the presence of 10-70% by weight of water based on the total amount of the substances used.

Assignments (3)
CHANGE OF NAME Recorded Sep 18, 2019
From: AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
To: NOURYON CHEMICALS INTERNATIONAL B.V.
Reel/Frame 050426/0671 →
SECURITY INTEREST Recorded Oct 1, 2018
From: STARFRUIT US MERGER SUB 1 LLC; STARFRUIT US MERGER SUB 2 LLC; AKZO NOBEL SURFACE CHEMISTRY LLC; AKZO NOBEL CHEMICALS B.V.; AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
To: WILMINGTON TRUST (LONDON) LIMITED, AS COLLATERAL AGENT
Reel/Frame 047231/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 13, 2017
From: AKZO NOBEL N.V.
To: AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
Reel/Frame 044427/0759 →