Integrated carboxylic acid production from synthesis gas

US2024010596A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2024010596-A1
Application numberUS-202118253605-A
CountryUS
Kind codeA1
Filing dateNov 17, 2021
Priority dateDec 1, 2020
Publication dateJan 11, 2024
Grant date

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

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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.

First claim

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.

Assignees

Inventors

Classifications

  • C07C51/225Primary

    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

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What does patent US2024010596A1 cover?
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 st…
Who is the assignee on this patent?
Rohm & Haas
What technology area does this patent fall under?
Primary CPC classification C07C51/225. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Jan 11 2024 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).