Bidentate ligands for hydroformylation of ethylene
US-9795952-B2 · Oct 24, 2017 · US
US11370737B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11370737-B2 |
| Application number | US-202117480265-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 21, 2021 |
| Priority date | Sep 25, 2020 |
| Publication date | Jun 28, 2022 |
| Grant date | Jun 28, 2022 |
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 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.
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.
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
Related publications grouped by family.
Answers are generated from the same data shown on this page.