Catalytic system for the production of olefins
Catalytic system for partial oxidation reactions of hydrocarbons characterized in that it contains: one or more metals belonging to the 1 st , 2 nd , and 3 rd transition series; one or more elements of group IIIA, IVA or VA, wherein at least one of said metals or said elements is in the form of a nitride.
1. A catalytic system for a catalytic partial oxidation reaction of a hydrocarbon, comprising:
one or more nitrides selected from the group consisting of Co 3 N, Cr 2 N, Fe 4 N, Mn 4 N, MoN, WN, VN, Si 3 N 4 , a Si—N—B system, a Si—B—N—C system, an oxynitride and mixtures thereof; and
a combination of at least two metals deposited on said nitrides,
wherein said combination is selected from the group consisting of Pt—Sn, Pt—Ga, Pt—Cu and Pt—Sn—Ga.
2. The catalytic system according to claim 1 , comprising from 0.05 to 15% by weight of said combination of metals.
3. A process for the production of an olefin from a gaseous paraffinic hydrocarbon, comprising:
partially oxidizing said hydrocarbon with a gas containing molecular oxygen in the presence of a catalytic system according to claim 1 , to obtain said olefin,
wherein said hydrocarbon has 2 to 6 carbon atoms.
4. The process according to claim 3 , wherein the partial oxidation is effected at a temperature ranging from 450 to 1000° C., at a pressure ranging from 1 to 15 Atm and a space velocity ranging from 5000 to 800000 h −1 .
5. The process according to claim 3 , wherein the partial oxidation is carried out using a reactor in which a gas inlet zone and a catalytic zone either have a tubular shape or a sand-glass shape or a truncated-conical shape.
6. The process according to claim 5 , wherein a stream of oxygen, air or enriched air and a fuel not having the function of directly producing an olefin is sent into the gas inlet zone and a gaseous stream of paraffinic hydrocarbon is sent into the catalytic zone.
7. The process according to claim 5 , wherein in the tubular-shaped or sand-glass shaped or truncated-conical shaped reactor, the catalyst fillings are differentiated so as to have two or three catalytic beds in series.
8. The process according to claim 7 , wherein a catalytic bed upstream consists of Pt deposited on said nitride and a catalytic bed down-stream consists of Pt, Sn and Ga deposited on said nitride.
9. The process according to claim 7 , wherein a catalytic bed upstream consists of Pt and Cu deposited on said nitride and a catalytic bed down-stream consists of Pt, Sn and Ga deposited on said nitride.
10. The process according to claim 7 , wherein a catalytic bed upstream consists of Pt deposited on said nitride, an intermediate catalytic bed consists of Pt and Sn deposited on said nitride, and a catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.
11. The process according to claim 7 , wherein a catalytic bed upstream consists of Pt and Cu deposited on said nitride, an intermediate catalytic bed consists of Pt, Sn and Bi deposited on said nitride, and a catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.
12. The process according to claim 7 , wherein a catalytic bed upstream consists of Pt deposited on said nitride, an intermediate catalytic bed consists of Pt and Sn deposited on said nitride, and a catalytic bed downstream consists of Pt, Sn and Sb deposited on said nitride.
13. The process according to claim 7 , wherein a catalytic bed upstream consists of Pt and Cu deposited on said nitride, an intermediate catalytic bed consists of Pt, Sn and Cr deposited on said nitride, and a catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.
14. The process according to claim 7 , wherein a catalytic bed upstream consists of Pt and Sn deposited on said nitride, an intermediate catalytic bed consists of Pt and Sn deposited on said nitride, and a catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.
15. A process for the production of an olefin from a gaseous paraffinic hydrocarbon, comprising:
partially oxidizing said hydrocarbon with a gas containing molecular oxygen in the presence of a catalytic system according to claim 1 ;
wherein said oxidation is effected at a temperature ranging from 450 to 1000° C., at a pressure ranging from 1 to 15 Atm and at a space velocity ranging from 5000 to 800000 h −1 in a reactor in which a gas inlet zone and a catalytic zone either have a tubular shape or a sand-glass shape or a truncated-conical shape;
wherein a stream of oxygen, air or enriched air and a fuel not having the function of directly producing an olefin is sent into the gas inlet zone and a gaseous stream of paraffinic hydrocarbon is sent into the catalytic zone.
16. The process according to claim 6 , wherein the fuel not having the function of directly producing olefin is selected from the group consisting of i) natural gas, ii) synthesis gas, iii) hydrogen and iv) a mixture of hydrogen and CO.
17. The process according to claim 15 , wherein the fuel not having the function of directly producing an olefin is selected from the group consisting of i) natural gas, ii) synthesis gas, iii) hydrogen and iv) a mixture of hydrogen and CO.