Catalysts for conversion of CO
View Patent ↗A catalytic method for producing gaseous products from a fuel and a gaseous reagent having the steps of: providing a catalyst and the fuel to a reactor vessel such that the catalyst and the fuel are in fluid communication with each other within the reactor vessel, where the catalyst is a mixture of reduced metal oxides; and contacting the fuel and catalyst with the gaseous reagent within the reactor vessel at a reaction temperature to produce gaseous products, where the gaseous reagent contains at least CO 2 or H 2 O, where the fuel comprises a carbonaceous source, and wherein the gaseous products are CO or syngas.
1 . A catalytic method for producing gaseous products from a fuel and a gaseous reagent comprising:
providing a catalyst and the fuel to a reactor vessel such that the catalyst and the fuel are in fluid communication with each other within the reactor vessel, wherein the catalyst comprises reduced metal aluminate compounds, wherein the reduced metal aluminate compounds are selected from the group consisting of Cu x —Al m —O p , Fe y —Al m —O p , Fe y —Mn z —Al m —O p , Cu x —Fe y —Al m —O p , Cu x —Mn z —Al m —O p , Cu x —Fe y —Mn z —Al m —O p , and combinations thereof, wherein 5≥x>0, 5≥y>0, 5≥z>0, 5≥m>0, and 4≥p>0; and
contacting the fuel and catalyst with the gaseous reagent supplied from an external source within the reactor vessel at a reaction temperature to produce gaseous products, wherein the gaseous reagent comprises CO 2 , wherein the fuel comprises a carbonaceous source, and wherein the gaseous products comprise CO.
2 . The method of claim 1 wherein the carbonaceous source is selected from the group consisting of coal, biomass, biooil, coke, biochar, methane, plastics and combinations thereof.
3 . The method of claim 1 wherein the gaseous reagent further comprises H 2 O, and wherein the gaseous products further comprise H 2 .
4 . The method of claim 1 wherein the catalyst and fuel are provided separately.
5 . The method of claim 1 wherein the carbonaceous source is a solid selected from the group consisting of coal, biochar, coke, biomass, plastics and combinations thereof, wherein the gaseous reagent is a combination of CO 2 and H 2 O, and wherein the gaseous products comprise a stream of CO and H 2 free from nitrogen.
6 . The method of claim 1 wherein the fuel comprises CH 4 , wherein the gaseous reagent comprises CO 2 , and wherein the gaseous products comprise a stream of H 2 and CO free from nitrogen.
7 . The method of claim 1 wherein the catalyst and fuel are not mixed or chemically intermingled prior to being provided to the reactor vessel.
8 . The method of claim 1 wherein the reduced metal aluminate compounds are selected from the group consisting of Cu—Fe—Mn—Al—O p , Cu—Fe 2 —Al—O p , Cu—Fe 1.5 —Al—O p , Fe 2.5 —Al 0.5 —O p , Cu—Al—O p , and combinations thereof, where 4≥p>0.
9 . The method of claim 1 wherein the fuel and gaseous reagent are provided to the reactor vessel continuously.
10 . A catalytic method for producing syngas products from a carbonaceous source and gaseous reagent comprising:
providing the carbonaceous source and a catalyst to a reactor vessel, wherein the catalyst comprises reduced metal aluminate compounds selected from the group consisting of Cu x —Al m —O p , Fe y —Al m —O p , Fe y —Mn z —Al m —O p , Cu x —Fe y —Al m —O p , Cu x —Mn z —Al m —O p , Cu x —Fe y —Mn z —Al m —O p , and combinations thereof, wherein 5≥x>0, 5≥y>0, 5≥z>0, 5≥m>0, and 4≥p>0; and
contacting the carbonaceous source and catalyst with a gaseous reagent to generate gaseous products where the gaseous reagent comprises CO 2 supplied from an external source and a gaseous product that comprises a product stream of at least 25% by volume CO.
11 . The method of claim 10 wherein the gaseous reagent comprises CO 2 and H 2 O, and wherein the gaseous products comprise CO and H 2 .
12 . The method of claim 10 wherein the gaseous reagent comprises H 2 O, and wherein the gaseous products comprise CO and H 2 .
13 . The method of claim 10 wherein the reduced metal aluminate compounds are selected from the group consisting of Cu—Fe—Mn—Al—O p , Cu—Fe 2 —Al—O p , Cu—Fe 1.5 —Al—O p , Fe 2.5 —Al 0.5 —O p , Cu—Al—O p , and combinations thereof, where 4≥p>0.
14 . The method of claim 10 wherein the carbonaceous source and catalyst are not chemically intermingled prior to being introduced to the reactor vessel.
15 . The method of claim 10 wherein the carbonaceous source comprises CH 4 , wherein the gaseous reagent comprises CO 2 , and wherein the gaseous product comprises CO and H 2 .
16 . The method of claim 10 wherein the carbonaceous source is a solid selected from the group consisting of coal, biochar, coke, biomass, plastics and combinations thereof, wherein the gaseous reagent is CO 2 , and wherein the gaseous product comprises a stream of CO free from nitrogen.
17 . The method of claim 10 wherein the carbonaceous source is a solid selected from the group consisting of coal, biochar, coke, biomass, plastics and combinations thereof, wherein the gaseous reagent is a combination of CO 2 and H 2 O, and wherein the gaseous product comprises a stream of CO and H 2 free from nitrogen.
18 . The method of claim 1 wherein the catalyst is calcined above about 1000° C.
19 . The method of claim 10 wherein the catalyst is calcined above about 1000° C.