Catalyst for reforming tar used in the steam gasification of biomass
US-9221033-B2 · Dec 29, 2015 · US
US2016332874A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016332874-A1 |
| Application number | US-201515109725-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 6, 2015 |
| Priority date | Jan 6, 2014 |
| Publication date | Nov 17, 2016 |
| Grant date | — |
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Processes for making a syngas mixture including hydrogen, carbon monoxide, and carbon dioxide are provided. In an exemplary embodiment, the processes include contacting a gaseous feed mixture that includes carbon dioxide, hydrogen and methane with a metal oxide catalyst that includes molybdenum and nickel. Catalysts for making a syngas mixture, including molybdenum and nickel are also provided.
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I/We claim: 1 . A process of making a syngas mixture comprising hydrogen and carbon monoxide, comprising: contacting a gaseous feed mixture that comprises carbon dioxide, hydrogen, and methane with a metal oxide catalyst comprising molybdenum and nickel to produce the syngas mixture. 2 . The process of claim 1 , wherein the process is carried out at a temperature of about 600° C. to about 800° C. 3 . The process of claim 1 , wherein the metal oxide catalyst further comprises a support material. 4 . The process of claim 3 , wherein the support material is selected from the group consisting of aluminum oxide, magnesium oxide, lanthanum oxide, and silica. 5 . The process of claim 1 , wherein the syngas mixture further comprises methane and carbon dioxide. 6 . The process of claim 1 , wherein the syngas mixture has a stoichiometric number of about 1.0 to about 3.0. 7 . The process of claim 1 , wherein the carbon dioxide, methane, and hydrogen and are present in the gaseous feed mixture in a ratio of about 1.0:1.0:2.0. 8 . The process of claim 1 , wherein the process is carried out at a temperature of about 720° C. 9 . The process of claim 1 , wherein the process is carried out at atmospheric pressure. 10 . The process of claim 1 , wherein the contact time for contacting the gaseous feed mixture with the catalyst is about 0.5 seconds to about 7.5 seconds. 11 . A catalyst for making a syngas mixture, comprising molybdenum and nickel, wherein the molybdenum is present in an amount of about 2 wt % to about 20 wt % and the nickel is present in an amount of about 2 wt % to about 25 wt %, based upon a total weight of the catalyst. 12 . The catalyst of claim 11 , wherein the catalyst further comprises a support. 13 . The catalyst of claim 12 , wherein the support material is selected from the group consisting of aluminum oxide, magnesium oxide, lanthanum oxide, and silica. 14 . The process of claim 1 , wherein the nickel is present in an amount of 12 wt % to about 15 wt %, based upon a total weight of the catalyst. 15 . A process of making a syngas mixture comprising hydrogen and carbon monoxide, comprising: contacting a gaseous feed mixture that comprises carbon dioxide, hydrogen, and methane with a metal oxide catalyst to produce the syngas mixture; wherein the process is carried out at a temperature of about 600° C. to about 800° C.; and wherein the metal oxide catalyst comprises molybdenum in an amount of about 2 wt % to about 20 wt % and nickel in an amount of about 2 wt % to about 25 wt %, based upon a total weight of the metal oxide catalyst. 16 . The process of claim 15 , wherein the process is carried out at atmospheric pressure. 17 . The process of claim 16 , wherein the contact time for contacting the gaseous feed mixture with the catalyst is about 0.5 seconds to about 7.5 seconds. 18 . The process of claim 15 , wherein the contact time for contacting the gaseous feed mixture with the catalyst is about 0.5 seconds to about 7.5 seconds.
using catalysts, e.g. selective catalysts · CPC title
Increasing the carbon monoxide content, e.g. reverse water-gas shift [RWGS] · CPC title
Nickel catalysts · CPC title
Composition of the catalyst · CPC title
Alkali or alkaline earth metals · CPC title
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