Catalytic system for the production of olefins

Abstract

Catalytic system for partial oxidation reactions of hydro-carbons 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 - 25 . (canceled)  
     
     
         26 . A catalytic system for a catalytic partial oxidation reaction of a hydrocarbon, comprising: 
 one or more nitrides selected from the group consisting of AlN, Co 3 N, Cr 2 N, Fe 4 N, Mn 4 N, MoN, TiN, 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.    
     
     
         27 . The catalytic system according to  claim 26 , comprising from 0.05 to 15% by weight of said combination of metals.  
     
     
         28 . 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 26 , to obtain said olefin,    wherein said hydrocarbon has 2 to 6 carbon atoms.    
     
     
         29 . The process according to  claim 28 , 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 .  
     
     
         30 . The process according to  claim 28 , 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.  
     
     
         31 . The process according to  claim 30 , 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.  
     
     
         32 . The process according to  claim 30 , 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.  
     
     
         33 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt deposited on said nitride and the catalytic bed down-stream consists of Pt, Sn and Ga deposited on said nitride.  
     
     
         34 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt and Cu deposited on said nitride and the catalytic bed down-stream consists of Pt, Sn and Ga deposited on said nitride.  
     
     
         35 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt and Ni deposited on said nitride and the catalytic bed down-stream consists of Pt, Sn and Cr deposited on said nitride.  
     
     
         36 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt deposited on said nitride, the intermediate catalytic bed consists of Pt and Sn deposited on said nitride, and the catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.  
     
     
         37 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt and Cu deposited on said nitride, the intermediate catalytic bed consists of Pt, Sn and Bi deposited on said nitride, and the catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.  
     
     
         38 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt deposited on said nitride, the intermediate catalytic bed consists of Pt and Sn deposited on said nitride, and the catalytic bed downstream consists of Pt, Sn and Sb deposited on said nitride.  
     
     
         39 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt and Cu deposited on said nitride, the intermediate catalytic bed consists of Pt, Sn and Cr deposited on said nitride, and the catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.  
     
     
         40 . The process according to  claim 32 , wherein the catalytic bed upstream consists of Pt and Sn deposited on said nitride, the intermediate catalytic bed consists of Pt and Sn deposited on said nitride, and the catalytic bed downstream consists of Pt, Sn and Ga deposited on said nitride.  
     
     
         41 . 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 26;     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.    
     
     
         42 . The process according to  claim 31 , 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.  
     
     
         43 . 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, to obtain said olefin,    wherein said hydrocarbon has 2 to 6 carbon atoms,    wherein said catalytic system comprises:    one or more metals selected from the group consisting of Pt, Cr, Mo, Cu, W, Ru, Zn, Ag, Au, Rh, Mn, Fe, Co, Ni and mixtures thereof;    one or more elements selected from the group consisting of Al, Sn, Ga, Pb, Sb, Bi, Si and mixtures thereof;    wherein at least one of said metals or said elements is present in form of a nitride selected from the group consisting of Co 3 N, Cr 2 N, Fe 4 N, Mn 4 N, MoN, WN, VN, a Si—N—B system, a Si—B—N—C system, an oxynitride and mixtures thereof.    
     
     
         44 . 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;    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,    wherein said catalytic system comprises:    one or more metals selected from the group consisting of Pt, Cr, Mo, Cu, W, Ru, Zn, Ag, Au, Rh, Mn, Fe, Co, Ni and mixtures thereof;    one or more elements selected from the group consisting of Al, Sn, Ga, Pb, Sb, Bi, Si and mixtures thereof;    wherein at least one of said metals or said elements is present in form of a nitride selected from the group consisting of Co 3 N, Cr 2 N, Fe 4 N, Mn 4 N, MoN, WN, VN, a Si—N—B system, a Si—B—N—C system, an oxynitride and mixtures thereof.    
     
     
         45 . The process according to  claim 41 , 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.