Solid-supported palladium(ii) complex for catalyzing mizoroki-heck coupling reactions and a method thereof
US-2018065117-A1 · Mar 8, 2018 · US
US10150109B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10150109-B2 |
| Application number | US-201815919812-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 13, 2018 |
| Priority date | Sep 6, 2016 |
| Publication date | Dec 11, 2018 |
| Grant date | Dec 11, 2018 |
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A solid-supported palladium(II) complex which catalyzes the Mizoroki-Heck coupling reaction efficiently and a method of employing the solid-supported palladium(II) complex to synthesize cinnamic acid and derivatives thereof. The solid-supported palladium(II) complex is also stable and can be recycled without significantly losing catalytic activity.
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The invention claimed is: 1. A silica-supported catalyst, comprising a reaction product of: a ligand of formula (I) a solid silica support; wherein X is O, R 1 and R 2 are each independently optionally substituted alkyl, R 3 , R 4 , R 5 and R 6 are H, n is 1; and a palladium(II) salt of the formula PdCl 2 ; wherein the solid silica support is functionalized to comprise a substituted benzyl group and X is bonded to a carbon atom of the benzyl group in the reaction product; wherein the reaction product comprises a palladium(II) ion bound to a nitrogen atom in each oxazoline heterocycle in formula (I). 2. The silica-supported catalyst of claim 1 , wherein the solid silica support is in the form of a particle with an average diameter of 1-100 μm. 3. The silica-supported catalyst of claim 1 , which comprises 0.1-1 mmol of palladium per gram of the silica-supported catalyst. 4. The silica-supported catalyst of claim 1 , which has a turnover number in a range of 1,500-2,500 and a turnover frequency in a range of 200-1,500 per hour. 5. A method for synthesizing cinnamic acid or derivatives thereof, the method comprising: reacting an aryl halide with an acrylic acid or derivatives thereof in the presence of a solvent, a base, and the silica-supported catalyst of claim 1 at a temperature in a range of 35-110° C., thereby forming the cinnamic acid or derivatives thereof. 6. The method of claim 5 , further comprising: separating the silica-supported catalyst from the cinnamic acid or derivatives thereof; and reusing the silica-supported catalyst in at least two cycles, wherein the silica-supported catalyst loses less than 5 wt % of the palladium after the at least two cycles. 7. The method of claim 5 , wherein the aryl halide is a limiting reactant. 8. The method of claim 5 , wherein an amount of the silica-supported catalyst is in a range of 0.05-10 mol % relative to a number of moles of the aryl halide. 9. The method of claim 5 , wherein the solvent comprises 5-95% by volume of water and 5-95% by volume of an organic solvent, based on a total volume of the solvent. 10. The method of claim 5 , wherein the base is at least one selected from the group consisting of an alkali metal hydroxide, an alkali metal carbonate, and an amine.
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