Catalyst for the synthesis of methyl mercaptan and process for producing methyl mercaptan from synthesis gas and hydrogen sulphide
View Patent ↗The invention relates to a catalyst comprising an active component based on molybdenum and on potassium and a support based on hydroxyapatite, and also to a process for preparing said catalyst and a process for producing methyl mercaptan in a catalytic process by reaction of carbon monoxide, sulphur and/or hydrogen sulphide and hydrogen, comprising the use of said catalyst.
1. A process for producing methyl mercaptan in a catalytic process by reacting carbon oxide, sulfur and/or hydrogen sulfide and hydrogen, comprising using a catalyst comprising a molybdenum- and potassium-based active component and a hydroxyapatite-based support.
2. The process of claim 1 , wherein the hydroxyapatite of the hydroxyapatite-based support has a Ca/P molar ratio ranging from 1.5 to 2.1.
3. The process of claim 1 , wherein the hydroxyapatite of the hydroxyapatite-based support has, a Ca/P molar ratio of 1.67.
4. The process of claim 1 , wherein the hydroxyapatite-based support specific area greater than 25 m 2 /g.
5. The process of claim 1 , wherein the hydroxyapatite-based support has a specific area greater than 40 m 2 /g.
6. The process of claim 1 , wherein h catalyst support is hydroxyapatite having stoichiometric formula Ca 10 (PO 4 ) 6 (OH) 2 .
7. The process of claim 6 , wherein the molybdenum- and potassium-based active component is selected from the group consisting of compounds based on Mo—S—K, compounds based on Mo—O—K, and their mixtures.
8. The process of claim 7 , wherein the molybdenum- and potassium- sed active component has been obtained from a precursor having structure K 2 MoS 4 .
9. The process of claim 8 , wherein the weight ratio of K 2 MoS 4 and Ca 10 (PO 4 ) 6 (OH) 2 used to obtain the catalyst is:
K 2 MoS 4 /Ca 10 (PO 4 ) 6 (OH) 2 =31.3/100.
10. The process of claim 7 , wherein the molybdenum and potassium-based active component has been obtained from a precursor having structure K 2 MoS 4 .
11. The process of claim 10 , wherein the weight ratio of K 2 MoS 4 and Ca 10 (PO 4 ) 6 (OH) 2 used to obtain the catalyst is:
K 2 MoO 4 /Ca 10 (PO 4 ) 6 (OH) 2 =50.7/100.
12. The process of claim 1 , wherein the hydroxyapatite is a stoichiometric hydroxyapatite.
13. The process of claim 1 , wherein the catalyst does not include a promoter.
14. The process of claim 1 , wherein the catalyst includes a promoter.
15. The process of claim 1 , wherein the carbon oxide is CO or CO 2 .
16. The process of claim 15 , wherein the CO or CO 2 /H 2 S/H 2 molar ratios range from 1/1/0 to 1/8/8.
17. The process of claim 15 , wherein the molar ratios of CO or CO 2 /H 2 S/H 2 /S reagents range from 1/1/0/1 to 1/8/8/8.
18. The process of claim 15 , wherein the CO or CO 2 /H 2 S/H 2 molar ratios range from 1/2/1 to 1/4/4.
19. The process of claim 15 , wherein the molar ratios of CO or CO 2 /H 2 S/H 2 /S reagents range from 1/2/2/1 to 1/4/4/4.
20. The process of claim 1 , wherein the catalyst is prepared by a process comprising:
preparing a precursor for the molybdenum- and potassium-based active component;
preparing the hydroxyapatite-based support; and,
dry impregnating the hydroxyapatite-based support with the precursor for the molybdenum- and potassium-based active component.