Alpha,Alpha-Difluoroacetaldehyde Production Method
US-2015329455-A1 · Nov 19, 2015 · US
US9944579B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9944579-B2 |
| Application number | US-201615544243-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 15, 2016 |
| Priority date | Jan 15, 2015 |
| Publication date | Apr 17, 2018 |
| Grant date | Apr 17, 2018 |
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A phosphorus ligand-free, mild, efficient and complete catalytic hydrogenation process is for the sustainable production of terminal diols from renewable terminal dialkyl esters with improved yield. Soluble, phosphorus ligand free Ru (II)-pincer type complexes can be used as catalysts in the hydrogenation process.
Opening claim text (preview).
We claim: 1. A catalytic hydrogenation process for synthesis of terminal diols starting from terminal dialkyl aliphatic esters, comprising, stirring a reaction mixture of phosphorus free catalyst, potassium tert-butoxide ( t BuOK), terminal dialkyl aliphatic esters and toluene at temperature of 110° C. for a period in the range of 22 to 24 hr under H 2 pressure, wherein said catalyst is selected from the group consisting of HCl(CO)Ru( isoPr SNS) (2), HCl(CO)Ru( Ph SNS) (4), and HCl(CO)Ru( Et SNS) (5), represented by the formula 2. The process as claimed in claim 1 , wherein said terminal dialkyl aliphatic ester is selected from the group consisting of dialkyl oxalate, dialkyl malonate, dialkyl succinate, diethyl glutarate and dialkyl adipate, wherein alkyl groups in said terminal dialkyl aliphatic ester is linear or branched. 3. The process as claimed in claim 1 , wherein said terminal diol is selected from the group consisting of ethane-1,2-diol, propane-1,3-diol, butane-1,4-diol, pentane-1,5-diol, and hexane-1,6-diol. 4. The process as claimed in claim 1 , wherein a yield of said terminal diols is in the range of 35-70%. 5. A phosphorus-free catalyst of formula 4: 6. A process for the preparation of phosphorus free catalyst selected from the group consisting of HCl(CO)Ru( isoPr SNS) (2), HCl(CO)Ru( Ph SNS) (4), and HCl(CO)Ru( Et SNS) (5), represented by the formula wherein said process comprises: (a) adding a methanolic solution of sodium thiolate compound and potassium hydroxide (KOH) to a solution of bis (2-chloroethyl)amine hydrochloride in methanol followed by stirring for 12 to 14 hrs at 30° C. to afford corresponding SNS compounds; and (b) refluxing the reaction mixture of compound of step (a), RuHCl(CO)(PPh 3 ) 3 and o-xylene at temperature ranging from 140 to 150° C. for a period ranging from 1 to 2 hr under argon atmosphere to yield Ru (II)-pincer type SNS complexes. 7. The process as claimed in claim 6 , wherein said sodium thiolate compound is selected from the group consisting of sodium-2-propanethiolate, sodium thiophenolate and sodium ethanethiolate. 8. The process as claimed in claim 6 , wherein said SNS compounds are selected from the group consisting of bis (2-(phenylthio) ethyl) amine [ Ph SNS] (3), bis(2-(isopropylthio)ethyl)amine [ isoPr SNS] (1) and bis (2-(ethylthio) ethyl) amine [ Et SNS]. 9. The process as claimed in claim 6 , wherein said Ru (II)-pincer type SNS complexes is selected from the group consisting of HCl(CO)Ru( isoPr SNS) (2), HCl(CO)Ru( Ph SNS) (4), and HCl(CO)Ru(Et-SNS) (5).
with hydrogen or hydrogen-containing gases · CPC title
Sulfur, e.g. thiocarbamates · CPC title
Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes · CPC title
Ruthenium · CPC title
the ligands containing nitrogen · CPC title
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