Alcohol mixtures including linear tridecanols
US-2024391857-A1 · Nov 28, 2024 · US
US9809518B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9809518-B2 |
| Application number | US-201615352851-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2016 |
| Priority date | Nov 20, 2015 |
| Publication date | Nov 7, 2017 |
| Grant date | Nov 7, 2017 |
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Butanediol production processes are described herein. In some embodiments, the processes include contacting an allyl alcohol stream with a hydroformylation catalyst in the presence of a gas stream including carbon monoxide and hydrogen under hydroformylation conditions sufficient to form a hydroformylation product stream including a butanediol intermediate, wherein the allyl alcohol stream includes less than 98 wt. % allyl alcohol.
Opening claim text (preview).
What is claimed is: 1. A process comprising: contacting an allyl alcohol stream with a hydroformylation catalyst comprising rhodium phosphate at a feed concentration of 0.3-3.3 wt. % in the presence of a gas stream comprising carbon monoxide and hydrogen under hydroformylation conditions sufficient to form a hydroformylation product stream comprising a butanediol intermediate, wherein the allyl alcohol stream comprises less than 98 wt. % allyl alcohol. 2. The process of claim 1 , further comprising contacting the butanediol intermediate with a hydrogenation catalyst in the presence of hydrogen under hydrogenation conditions sufficient to form a hydrogenation product stream comprising 1,4-butanediol. 3. The process of claim 2 , characterized by an allyl alcohol conversion of 80-100%. 4. The process of claim 2 , characterized by a selectivity of 65-100%. 5. The process of claim 2 , further comprising recovering 1,4-butanediol from the hydrogenation product stream. 6. The process of claim 1 , wherein the allyl alcohol stream comprises one or more impurities selected from acetone, water, propionaldehyde, n-propanol, C 4+ hydrocarbons, C 1+ oxygenates and combinations thereof. 7. The process of claim 6 , wherein the allyl alcohol stream comprises an acetone concentration in a range of 0 wt. % to 25 wt. % based on the total weight of the allyl alcohol stream, a water concentration in a range of 0 wt. % to 6 wt. % based on the total weight of the allyl alcohol stream, a propionaldehyde concentration in a range of 0 wt. % to 6 wt. % based on the total weight of the allyl alcohol stream, a n-propanol concentration in a range of 0 wt. % to 1 wt. % based on the total weight of the allyl alcohol stream, a C 4+ hydrocarbon concentration in a range of 0 wt. % to 5 wt. % based on the total weight of the allyl alcohol stream and C 1+ oxygenates concentration in a range of 0 wt. % to 11 wt. % based on the total weight of the allyl alcohol stream. 8. The process of claim 1 , wherein the allyl alcohol stream comprises methanol in a methanol concentration of less than 100 ppm. 9. The process of claim 1 , wherein the allyl alcohol stream comprises an acetone concentration of at least 0.25 wt. % based on the total weight of the allyl alcohol stream, a methanol concentration of less than 100 ppm based on the total weight of the allyl alcohol stream, a water concentration of at least 0.1 wt. % based on the total weight of the allyl alcohol stream, a propionaldehyde concentration of at least 0.25 wt. % based on the total weight of the allyl alcohol stream, or combinations thereof. 10. The process of claim 1 , wherein the hydroformylation conditions comprise a hydroformylation temperature in a range of 20° C. to 100° C. and a hydroformylation pressure in a range of 20 psig (137,895 Pa) to 600 psig (4,136,854 Pa). 11. The process of claim 1 , wherein the hydroformylation catalyst comprises a rhodium phosphate with a rhodium:phosphate molar ratio of 1:1-1.2:1.
by oxo-reactions · CPC title
with hydrogen or hydrogen-containing gases · CPC title
containing hydroxy groups (sugars C07H) · CPC title
1,4-Butanediol; 1,3-Butanediol; 1,2-Butanediol; 2,3-Butanediol · CPC title
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