Catalysts and Related Methods for Photocatalytic Production of H2O2 and Thermocatalytic Reactant Oxidation
US-2016272495-A1 · Sep 22, 2016 · US
US11266980B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11266980-B2 |
| Application number | US-201916508474-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 11, 2019 |
| Priority date | Jul 15, 2016 |
| Publication date | Mar 8, 2022 |
| Grant date | Mar 8, 2022 |
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A method for CO2 hydrogenation via the reverse water-gas shift (RWGS) reaction using alkali metal-doped molybdenum carbide, supported on gamma alumina (A-Mo2C/γ-Al2O3, A=K, Na, Li). The A-Mo2C/γ-Al2O3 catalyst is synthesized by co-impregnation of molybdemun and alkali metal precursors onto a γ-Al2O3 support. It is then carburized to form the A-Mo2C/γ-Al2O3. Also disclosed is the related catalyst material.
Opening claim text (preview).
What is claimed as new and desired to be protected by Letters Patent of the United States is: 1. A method for CO 2 hydrogenation via the reverse water-gas shift (RWGS) reaction for the selective formation of CO, comprising: co-impregnating molybdenum and alkali-metal precursors onto a γ-Al 2 O 3 support, wherein the alkali metal is K, Na, or Li; drying and calcining impregnated γ-Al 2 O 3 support; carburizing the dried and calcined γ-Al 2 O 3 support to form A-Mo 2 C/γ-Al 2 O 3 , wherein A is K, Na, or Li; and reacting the A-Mo 2 C/γ-Al 2 O 3 with CO 2 and H 2 to form CO. 2. The method of claim 1 , wherein the loading of Mo is in the range of 1 to 70 weight percent. 3. The method of claim 1 , wherein the loading of the alkali metal is in the range of 0.1 to 15 weight percent. 4. The method of claim 1 , wherein the carburization is performed at a temperature in the range of 400 to 1000° C. 5. The method of claim 1 , wherein the reaction is performed while applying external heat. 6. The method of claim 1 , wherein the reaction is performed at a temperature in the range of 250 to 1000° C. 7. The method of claim 1 , wherein the reaction is performed at a pressure between 0 and 350 psig. 8. The method of claim 1 , wherein the reaction is performed while flowing carbon dioxide, hydrogen gas, or any combination thereof, over the A-Mo 2 C/γ-Al 2 O 3 catalyst material. 9. The method of claim 1 , wherein the reaction is performed while applying external heat and flowing carbon dioxide, hydrogen gas, or any combination thereof, over the A-Mo 2 C/γ-Al 2 O 3 catalyst material. 10. The method of claim 1 , wherein the CO 2 hydrogenation via the RWGS reaction achieves a CO yield of 12% or greater. 11. The method of claim 1 , wherein the CO 2 hydrogenation via the RWGS reaction achieves a CO selectivity of 90% or greater.
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Carbides · CPC title
Impregnation · CPC title
Tungsten or molybdenum carbides · CPC title
Boron or aluminium; Oxides or hydroxides thereof · CPC title
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