Processes for improving the activity of hybrid catalysts
US-2020123078-A1 · Apr 23, 2020 · US
US12454496B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12454496-B2 |
| Application number | US-202118003800-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 18, 2021 |
| Priority date | Jun 30, 2020 |
| Publication date | Oct 28, 2025 |
| Grant date | Oct 28, 2025 |
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A process for preparing C2 to C3 hydrocarbons may include introducing a feed stream including hydrogen gas and a carbon-containing gas comprising carbon monoxide, carbon dioxide, and mixtures thereof into a reaction zone of a reactor, and converting the feed stream into a product stream comprising C2 to C3 hydrocarbons in the reaction zone in the presence of a hybrid catalyst. The hybrid catalyst may include a metal oxide catalyst component and a microporous catalyst component comprising 8-MR pore openings less than or equal to 5.1 A and a cage defining ring size less than or equal to 7.45 A, where a C2/C3 carbon molar ratio of the product stream is greater than or equal to 0.7.
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The invention claimed is: 1. A process for preparing C 2 to C 3 hydrocarbons comprising: introducing a feed stream comprising hydrogen gas and a carbon-containing gas selected from the group consisting of carbon monoxide, carbon dioxide, and mixtures thereof into a reaction zone of a reactor; and converting the feed stream into a product stream comprising C 2 to C 3 hydrocarbons in the reaction zone in the presence of a hybrid catalyst, the hybrid catalyst comprising: a mixed metal oxide catalyst component; and a microporous catalyst component comprising 8-MR pore openings having a size less than or equal to 5.1 {acute over (Å)} and a cage defining ring size less than or equal to 7.45 {acute over (Å)}, wherein: a C 2 /C 3 carbon molar ratio of the product stream is greater than or equal to 0.7. 2. The process of claim 1 , wherein the microporous catalyst component comprises one or more of silicaaluminate or silicoaluminophosphate (SAPO). 3. The process of claim 1 , wherein the microporous catalyst component comprises an Erionite or Levyne structure. 4. The process of claim 1 , wherein the microporous catalyst component comprises one or more of SAPO-17, SAPO-35, LZ-220, SSZ-17, SSZ-98, SSZ-105, SAPO-67, or combinations thereof. 5. The process of claim 1 , wherein the microporous catalyst component comprises a SiO 2 /Al 2 O 3 molar ratio less than or equal to 50.0. 6. The process of claim 1 , wherein the metal component comprises from 0.1 wt. % to 10.0 wt. % of the metal oxide catalyst component. 7. The process of claim 1 , wherein the mixed metal oxide catalyst component comprises a metal oxide support material comprising zirconia. 8. The process of claim 7 , wherein the mixed metal oxide catalyst component comprises gallium supported on zirconia. 9. The process of claim 1 , wherein the reaction zone operates at a temperature from 370° C. to 470° C. 10. The process of claim 1 , wherein the reaction zone operates at a pressure from 20 bar to 70 bar. 11. The process of claim 1 , wherein the gas hourly space velocity (GHSV) is greater than 500 hr −1 . 12. The process of claim 1 , wherein the hybrid catalyst comprises a metal oxide catalyst component to microporous catalyst component weight ratio of from 0.1:1 to 10:1. 13. The process of claim 1 , wherein the product stream comprises greater than 40 C mol % C 2 to C 3 hydrocarbons based on the total hydrocarbon fraction in the product stream. 14. The process of claim 1 , wherein the C 2 /C 3 carbon molar ratio of the product stream is greater than or equal to 1.0. 15. The process of claim 1 , wherein the C 2 to C 3 hydrocarbons consist essentially of olefins.
less than 2 nm · CPC title
of the type L · CPC title
of the eroionite or offretite type, e.g. zeolite T · CPC title
of gallium, indium or thallium · CPC title
Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof · CPC title
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