Catalyst for the synthesis of methyl mercaptan and process for producing methyl mercaptan from synthesis gas and hydrogen sulphide
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 catalyst comprising a molybdenum- and potassium-based active component and a hydroxyapatite-based support.
2. The catalyst of claim 1 , wherein the catalyst support is hydroxyapatite having stoichiometric formula Ca 10 (PO 4 ) 6 (OH) 2 .
3. The catalyst of claim 2 , 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 mixtures thereof.
4. The catalyst of claim 3 , wherein the molybdenum- and potassium-based active component is obtained from a precursor having the formula K 2 MOS 4 .
5. The catalyst of claim 4 , 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.
6. The catalyst of claim 3 , wherein the molybdenum- and potassium-based active component is obtained from a precursor having structure K 2 MoO 4 .
7. The catalyst of claim 6 , wherein the weight ratio of K 2 MoO 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.
8. The catalyst of claim 1 , wherein the hydroxyapatite of the hydroxyapatite-based support has a Ca/P molar ratio ranging from 1.5 to 2.1.
9. The catalyst of claim 1 , wherein the hydroxyapatite of the hydroxyapatite-based support has a Ca/P molar ratio of 1.67.
10. The catalyst of claim 1 , wherein the hydroxyapatite-based support has a specific area greater than 25 m 2 /g.
11. The catalyst of claim 1 , wherein the hydroxyapatite-based support has a specific area greater than 40 m 2 /g.
12. The catalyst of claim 1 , wherein the hydroxyapatite is a stoichiometric hydroxyapatite.
13. The catalyst of claim 1 , wherein the catalyst does not include a promoter.
14. The catalyst of claim 1 , wherein the catalyst further comprises a promoter.
15. The catalyst of claim 14 , wherein the promoter comprises at least one of tellurium oxide, nickel oxide or iron oxide.
16. The catalyst of claim 1 , wherein the hydroxyapatite-based support has a specific area of 40 m 2 /g to 300 m 2 /g.
17. The catalyst of claim 1 , wherein the hydroxyapatite-based support has a specific area of 40 m 2 /g to 300 m 2 /g and a Ca/P molar ratio of 1.67.
18. A process for preparing the catalyst of claim 1 , 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.