HYDROFORMYLATION CATALYST, COMPOSITION INCLUDING HYDROFORMYLATION CATALYST, AND METHOD OF PREPARING ALDEHYDE USING HYDROFORMYLATION CATALYST (As Amended)
US-2018290132-A1 · Oct 11, 2018 · US
US12281063B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12281063-B2 |
| Application number | US-202117798607-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 1, 2021 |
| Priority date | Feb 11, 2020 |
| Publication date | Apr 22, 2025 |
| Grant date | Apr 22, 2025 |
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 hydroformylation process for preparing 3,5,5-trimethylhexanal comprising reacting 2,4,4-trimethylpent-2-ene with H2 and CO in a reaction zone in the presence of one or more free organophosphite ligands of the general formula (I)wherein R1, R2, R3, R4 and R5 are each independently H, C1- to C9-alkyl or C1- to C9-alkoxy and R1, R2,R3, R4 and R5 are not H at the same time, andR6, R7, R8, R° and R1° are each independently H, C1- to C9-alkyl or C1- to C9-alkoxy and Re, R7,R8, R° and R1° are not H at the same time, andR11, R12, R13, R14 and R15 are each independently H, C1- to C9-alkyl or C1- to C9-alkoxy and R11,R12, R13, R14 and R15 are not H at the same time,and a homogeneous rhodium catalyst complexed with one or more organophosphite ligands of the general formula (I) at a pressure of 1 to 100 bar abs and a temperature of from 50 to 200° C.
Opening claim text (preview).
The invention claimed is: 1. A hydroformylation process for preparing 3,5,5-trimethylhexanal comprising reacting 2,4,4-trimethylpent-2-ene with H 2 and CO in a reaction zone in the presence of one or more free organophosphite ligands of general formula (I) wherein, R 1 , R 2 , R 3 , R 4 and R 5 are each independently H, C 1 - to C 9 -alkyl or C 1 - to C 9 -alkoxy and R 1 , R 2 , R 3 , R 4 and R 5 are not H at the same time, and R 6 , R 7 , R 8 , R 9 and R 10 are each independently H, C 1 - to C 9 -alkyl or C 1 - to C 9 -alkoxy and R 6 , R 7 , R 8 , R 9 and R 10 are not H at the same time, and R 11 , R 12 , R 13 , R 14 and R 15 are each independently H, C 1 - to C 9 -alkyl or C 1 - to C 9 -alkoxy and R 11 , R 12 , R 13 , R 14 and R 15 are not H at the same time, and a homogeneous rhodium catalyst complexed with one or more organophosphite ligands of the general formula (I) at a pressure of 1 to 100 bar abs and a temperature of from 50 to 200° C. 2. The process according to claim 1 , wherein a mixture comprising 2,4,4-trimethylpent-1-ene and 2,4,4-trimethylpent-2-ene is converted to 3,5,5-trimethylhexanal. 3. The process according to claim 2 , wherein the ratio of 2,4,4-trimethylpent-1-ene to 2,4,4-trimethylpent-2-ene in the mixture used is in the range from 99:1 to 1:99. 4. The process according to claim 1 , wherein the total amount of 2,4,4-trimethylpent-1-ene and 2,4,4-trimethylpent-2-ene of the total amount of olefin in the feed to the reaction zone is from 10 to 100%. 5. The process according to claim 1 , wherein the hydroformylation is carried out at a temperature of 80 to 150° C. 6. The process according to claim 1 , wherein the hydroformylation is carried out at a pressure of 5 to 80 bar abs. 7. The process according to claim 1 , wherein the molar ratio of the total amount of organophosphite ligands of the general formula (I) in the reaction zone to the total amount of rhodium in the reaction zone is in the range from 1:1 to 100:1. 8. The process according to claim 1 , wherein the rhodium concentration in the reaction zone is in the range of 20 to 250 ppmw based on the total weight of the liquid phase in the liquid phase in the reaction zone. 9. The process according to claim 1 , wherein the one or more organophosphite ligands of the general formula (I) are one or more of the following compounds: Organophosphite ligand of general R 2 , R 4 , R 5 , R 7 , R 9 , formula (I) R 1 , R 6 , R 11 R 3 , R 8 , R 13 R 10 , R 12 , R 14 , R 15 I) Methyl Methyl H II) Methyl H H III) Ethyl Ethyl H IV) Ethyl H H V) n-Propyl n-Propyl H VI) n-Propyl H H VII) Isopropyl Isopropyl H VIII) Isopropyl H H IX) n-Butyl n-Butyl H X) n-Butyl H H XI) sec-Butyl sec-Butyl H XII) sec-Butyl H H XIII) Isobutyl Isobutyl H XIV) Isobutyl H H XV) tert-Butyl tert-Butyl H XVI) tert-Butyl H H XVII) Methoxy Methoxy H XVIII) Methoxy H H XIX) Ethoxy Ethoxy H XX) n-Propoxy n-Propoxy H XXI) n-Propoxy H H XXII) Isopropoxy Isopropoxy H XXIII) Isopropoxy H H XXIV) n-Butoxy n-Butoxy H XXV) n-Butoxy H H XXVI) sec-Butoxy sec-Butoxy H XXVII) sec-Butoxy H H XXVIII) Isobutoxy Isobutoxy H XXIX) Isobutoxy H H XXX) tert-Butoxy tert-Butoxy H XXXI) tert-Butoxy H H XXXII) n-Nonyl H H. 10. The
with only carbon-to-carbon double bonds as unsaturation · CPC title
by oxo-reactions · CPC title
Asymmetric hydroformylation · CPC title
with hydroxyaryl compounds · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.