Production of products from natural resources
US-2019023640-A1 · Jan 24, 2019 · US
US2024010596A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024010596-A1 |
| Application number | US-202118253605-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 17, 2021 |
| Priority date | Dec 1, 2020 |
| Publication date | Jan 11, 2024 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A process for preparing C2 to C4 carboxylic acids from synthesis gas includes introducing a feed stream comprising hydrogen gas and a carbon-containing gas comprising carbon monoxide into a reaction zone of a first reactor, converting the feed stream into an intermediate stream comprising C2 to C4 hydrocarbons in the reaction zone in the presence of a first catalyst, wherein the intermediate stream further comprises carbon dioxide and wherein the first catalyst is a composite catalyst comprising a metal oxide catalyst component and a microporous catalyst component, and converting the intermediate stream into a product stream comprising C2 to C4 carboxylic acids in the presence of a second catalyst in a second reactor. The second reactor can be configured for olefin oxidation or paraffin oxidation.
Opening claim text (preview).
1 . A process comprising: introducing a feed stream comprising hydrogen gas and a carbon-containing gas comprising carbon monoxide and carbon dioxide into a reaction zone of a first reactor; converting the feed stream into an intermediate stream comprising C 2 to C 4 hydrocarbons in the reaction zone in the presence of a first catalyst, wherein the intermediate stream further comprises carbon dioxide and wherein the first catalyst is a composite catalyst comprising a metal oxide catalyst component and a microporous catalyst component; and converting the intermediate stream into a product stream comprising C 2 to C 4 carboxylic acids in the presence of a second catalyst in a second reactor. 2 . The process of claim 1 , wherein the intermediate stream comprising C 2 to C 4 hydrocarbons comprises C 2 to C 4 olefins, C 2 to C 4 paraffins, carbon dioxide, and unreacted carbon monoxide and hydrogen. 3 . The process of claim 2 , wherein the second reactor converts the C 2 to C 4 olefins in the intermediate stream to C 2 to C 4 carboxylic acids. 4 . The process of claim 3 , further comprising separating the C 2 to C 4 carboxylic acids and C 2 to C 4 paraffins from the product stream and recycling carbon dioxide and carbon monoxide to the feed stream. 5 . The process of claim 1 , wherein the metal oxide catalyst component comprises gallium oxide, zinc oxide, chromium oxide, zirconium oxide, or combinations thereof. 6 . The process of claim 5 , wherein the metal oxide catalyst component comprises gallium oxide and phase pure zirconium oxide. 7 . The process of claim 2 , wherein the second reactor converts the C 2 to C 4 paraffins in the intermediate stream to the product stream comprising C 2 to C 4 carboxylic acids. 8 . The process of claim 7 , further comprising separating the C 2 to C 4 carboxylic acids from the product stream and recycling carbon dioxide, carbon monoxide, and unreacted C 2 to C 4 paraffins to the feed stream. 9 . The process of claim 1 , wherein the metal oxide catalyst component comprises gallium oxide. 10 . The process of claim 1 , wherein unreacted hydrogen is removed from the intermediate stream prior to converting the intermediate stream into the product stream. 11 . The process of claim 1 , wherein the microporous catalyst component is a molecular sieve having 8-MR pore openings. 12 . The process of claim 1 , wherein the microporous catalyst component is a molecular sieve having a Chabazite (CHA) framework. 13 . The process of claim 1 , wherein the microporous catalyst component comprises SAPO-34. 14 . The process of claim 1 , wherein the microporous catalyst component comprises SSZ-13.
of paraffin waxes · CPC title
Separation; Purification; Stabilisation; Use of additives · CPC title
Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof · CPC title
of gallium, indium or thallium · CPC title
Silicoaluminophosphates (SAPO compounds) · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.