IP Library Granted Patent US 11,608,315
Granted Patent B2
US 11,608,315 · App. 16/956,201 · Granted Mar 21, 2023

Process for the preparation of methyl mercaptan

Inventors: Georges Frémy (Sauveterre de Bearn, FR); Hélori Salembier (Pau, FR); Carole Lamonier (Armentieres, FR); Pascal Blanchard (Lens, FR)
Assignees: Arkema France; Universite Lille 1-Sciences et Technologies; Centre National de la Recherche Scientifique (CNRS)
C07C319/06B01J21/066B01J23/28B01J35/1014C01B32/70C01B32/77C07C319/02C07C319/14C07C319/28C07C321/04
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Quick Facts
Patent No.
US 11,608,315
App. No.
16/956,201
Granted
Mar 21, 2023
Kind
B2
Abstract

The invention relates to a process for preparing methyl mercaptan from a mixture of carbon oxide, hydrogen sulfide and hydrogen, in the presence of a catalyst based on molybdenum and potassium supported on zirconia, said catalyst not comprising any promoter.

Claims (12)

1. A process for preparing methyl mercaptan (CH 3 SH), comprising:

a) reacting a carbon oxide, hydrogen sulphide (H 2 S) and hydrogen (H 2 ) in the presence of a zirconia-supported molybdenum- and potassium containing catalyst, the catalyst not comprising a promoter, to form a carbonyl sulphide;

b) hydrogenating the carbonyl sulphide obtained in step a) in the presence of the hydrogen, to form methyl mercaptan and hydrogen sulphide;

c) optionally, recycling the hydrogen sulphide formed in step b) to step a); and

d) collecting the methyl mercaptan.

2. The process according to claim 1 , wherein the zirconia-supported catalyst used in step a) comprises a molybdenum- and potassium containing active phase.

3. The process according to claim 1 , wherein the zirconia-supported molybdenum- and potassium-containing catalyst used in step a) is K 2 MoO 4 /ZrO 2 .

4. The process according to claim 1 , wherein the molybdenum- and potassium-containing catalyst is K 2 MoO 4 , where the catalyst comprises between 1% and 50% by weight, relative to the total weight of the catalyst and the zirconia support.

5. The process according to claim 1 , wherein the zirconia catalyst support has a specific surface area greater than 30 m 2 .g −1 .

6. The process according to claim 1 , wherein the carbon oxide is carbon monoxide (CO).

7. The process according to claim 1 , wherein the hydrogen sulphide formed in step b) is recycled in step a).

8. The process according to claim 1 , wherein the reaction temperature in step a) is between 100° C. and 500° C.

Assignments (2)
CHANGE OF ADDRESS Recorded Jul 4, 2025
From: ARKEMA FRANCE
To: ARKEMA FRANCE
Reel/Frame 071814/0739 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 6, 2020
From: FRÉMY, GEORGES; SALEMBIER, HÉLORI; LAMONIER, CAROLE; BLANCHARD, PASCAL
To: ARKEMA FRANCE; UNIVERSITÉ LILLE 1 - SCIENCES ET TECHNOLOGIES; CENTRE NATIONAL DE LA RECHERCHE SCIENTIFIQUE (CNRS)
Reel/Frame 053986/0020 →
Priority Claims (1)
FR 1763023 · Dec 22, 2017 · national
Continuity (1)
Related Publication 20200331852A1 · Oct 22, 2020