Co-feeding ethylene with allyl alcohol in hydroformylation to make 1,4-butanediol and n-propanol

US11370737B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11370737-B2
Application numberUS-202117480265-A
CountryUS
Kind codeB2
Filing dateSep 21, 2021
Priority dateSep 25, 2020
Publication dateJun 28, 2022
Grant dateJun 28, 2022

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Abstract

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A process of co-feeding gaseous ethylene with liquid allyl alcohol in the presence of a catalyst to produce 1,4-butanediol and n-propanol may include: introducing a gaseous mixture of ethylene, carbon monoxide and hydrogen into a reactor in the presence of a hydroformylation catalyst in a solvent; introducing liquid allyl alcohol (AA) into the reactor; and carrying out hydroformylation reaction at a temperature between 50 and 100° C. to obtain hydroformylation products.

First claim

Opening claim text (preview).

What is claimed is: 1. A method comprising the steps of: a) introducing a gaseous mixture of ethylene, carbon monoxide and hydrogen into a reactor in the presence of a hydroformylation catalyst in a solvent; b) introducing liquid allyl alcohol (AA) into the reactor; and c) carrying out hydroformylation reaction at a temperature between 50 and 100° C. to obtain hydroformylation products, wherein the hydroformylation products include 4-hydroxybutyraldehyde, 3-hydroyx-2-methylpropionaldehyde, propionaldehyde or a combination thereof. 2. The method of claim 1 , wherein the molar ratio of ethylene to allyl alcohol ranges from 1:3 to 1:7. 3. The method of claim 1 , wherein the molar ratio of ethylene to allyl alcohol ranges from 1:4 to 1:5. 4. The method of claim 1 , wherein the amount of allyl alcohol ranges between 10 and 25 wt. % concentration in the solvent, calculated by weight ⁢ ⁢ of ⁢ ⁢ AA weight ⁢ ⁢ of ⁢ ⁢ the ⁢ ⁢ solvent + AA × ⁢ 100 ⁢ % . 5. The method of claim 1 , wherein molar ratio of ethylene:carbon monoxide:hydrogen is (0.18-0.35):(2.7-4.1):(5-7). 6. The method of claim 1 , wherein the molar ratio of ethylene:carbon monoxide:hydrogen is about 1:13:22. 7. The method of claim 1 , wherein in step c) the hydroformylation reaction is carried out at a moderate pressure in the range of from about 137.9 kPa to about 1378.95 kPa. 8. The method of claim 1 , wherein in step c) the hydroformylation reaction is carried out at a moderate pressure in the range of from about 689.48 kPa to about 1034.21 kPa. 9. The method of claim 1 , wherein in step c) the hydroformylation reaction is carried out at a moderate pressure in the range of from about 896.32 kPa to about 965.27 kPa. 10. The method of claim 1 , wherein the hydroformylation catalyst is a mixture of rhodium and a ligand selected from the group consisting of trans-1,2-bis(3,5-trimethylphenylphosphinomethyl) cyclobutane (Ligand A), 1,4-bis(diphenylphosphinobutane) (DPPB), triphenylphosphine (TPP), bidentate biphosphate, and combinations thereof. 11. The method of claim 10 , wherein the molar ratio of rhodium to Ligand A ranges from 1:1 to 1:5. 12. The method of claim 10 , wherein the molar ratio of rhodium to Ligand A is about 1:2. 13. The method of claim 10 , wherein the hydroformylation catalyst is a mixture of rhodium, Ligand A, DPPB and TPP. 14. The method of claim 13 , wherein the molar ratio of rhodium:Ligand A:DPPB:TPP is about 1:2:0.1:2. 15. The method of claim 10 , wherein the rhodium is present in an amount of 50 to 500 ppm. 16. The method of claim 1 , wherein in step c) the temperature is between 50 and 80° C. 17. The method of claim 1 , further comprising the step of: separating the products from the solvent and the catalyst by water extraction. 18. The method of claim 17 , wherein a water-to-feed ratio ranges from 1:5 to 2:1. 19. The method of claim 1 , further comprising the step of: (d) treating the hydroformylation products include 4 -hydroxybutyraldehyde, 3-hydroxy-2-methylpropionaldehyde, and propionaldehyde with a Ni hydrogenation catalyst to produce a hydrogenation product, wherein the hydrogenation product includes, 1,4-butanediol, 2-methyl-1,3-propanediol, propanol or a combination thereof. 20. The method of claim 19 , wherein the hydroformylation catalyst is a mixture of rhodium and a ligand selected from the group consisting of trans-1,2-bis(3,5-trimethylphenylphosphinomethyl) cyclobutane (Ligand A), 1,4-bis(diphenylphosphinobutane) (DPPB), triphenylphosphine (TPP), bidentate biphosphate, and combinations thereof.

Assignees

Inventors

Classifications

  • with more than one complexing phosphine-P atom · CPC title

  • Rhodium · CPC title

  • with hydrogen or hydrogen-containing gases · CPC title

  • comprising aliphatic or saturated rings · CPC title

  • Hydroformylation, metalformylation, carbonylation or hydroaminomethylation · CPC title

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What does patent US11370737B2 cover?
A process of co-feeding gaseous ethylene with liquid allyl alcohol in the presence of a catalyst to produce 1,4-butanediol and n-propanol may include: introducing a gaseous mixture of ethylene, carbon monoxide and hydrogen into a reactor in the presence of a hydroformylation catalyst in a solvent; introducing liquid allyl alcohol (AA) into the reactor; and carrying out hydroformylation reaction…
Who is the assignee on this patent?
Lyondell Chemical Tech Lp
What technology area does this patent fall under?
Primary CPC classification B01J31/2414. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Jun 28 2022 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 2 related publications on this page (citations in our corpus or others sharing the same primary CPC).