Process for selectively hydroesterifying diolefin
AssigneeNippon Petrochemicals Company, Limited
InventorsIsoo Shimizu, Yasuo Matsumura, Yutaka Arai
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AssigneeNippon Petrochemicals Company, Limited
InventorsIsoo Shimizu, Yasuo Matsumura, Yutaka Arai
Estimating the term…
A process for selectively hydroesterifying a diolefin, which comprises reacting a (1-arylethenyl)vinylbenzene with carbon monoxide and water or a lower alcohol at a reaction temperature of 40.degree. to 200.degree. C. and a carbon monoxide pressure 20 to 700 kg/cm.sup.2 in the presence of a noble metal complex catalyst to thereby selectively hydroesterifying only the vinyl group of it and produce .alpha.-((1-arylethenyl)phenyl)propionic acid or its alkyl ester. The starting material to be hydroesterified may be a mixture of 1,1-di(substituted aryl)ethylene not substituted by a vinyl group.
A process for selective hydroesterification which is characterized in the step of reacting a (1-arylethenyl)vinylbenzene represented by the following formula (I) with carbon monoxide and water or a lower alcohol in the presence of a noble metal complex carbonylation catalyst at a temperature of 40.degree. to 200.degree. C. and a carbon monoxide pressure of 20 to 700 kg/cm.sup.2, thereby producing .alpha.-((1-arylethenyl)phenyl)propionic acid or its alkyl ester represented by the following formula (II), ##STR4## (in which Ar is a substituted aryl group which may have a substituent group other than vinyl group and R is a hydrogen atom or a lower alkyl group).
Dependencies are inferred from the claim text.
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Containing six-membered aromatic rings and other rings, e.g. cyclohexylphenylacetic acid: having unsaturation outside the aromatic rings
Starting from organic compounds containing only oxygen atoms as heteroatoms: by elimination of water
The hetero-atom being a metal atom: the hetero-atom being a magnesium atom
Catalytic processes: with metal oxides or metal sulfides
Term ended 14 Nov 2008 (estimated)
USPTO file history isn’t available for this patent, so only indexed dates are shown.
1. Technical Field
This invention relates to a process for selective hydroesterification. More particularly, the invention relates to a process for producing unsaturated acid or its ester by selectively hydroesterifying diolefin.
Furthermore, the invention relates to a process for selectively hydroesterifying only diolefin in a material which contains certain monoolefins.
The present invention is described in the following with reference to examples.
To a 2 liter three-neck flask equipped with a dropping funnel, a reflux condenser and a stirrer was added 25.5 g (1.05 mole) of metallic magnesium and it was dried sufficiently by supplying dry nitrogen gas. After that, 50 ml of tetrahydrofuran which had been dried with a molecular sieve 5A, was put into the flask and the contents were stirred vigorously. A solution of 183 g (1.0 mole) of 3-vinylbenzene bromide in 500 ml of dried tetrahydrofuran was then dropped little by little over 2 hours. The reaction temperature was maintained 75.degree. to 80.degree. C. and, after the addition of the solution, the stirring was continued for further 1 hour as it stands. Into the thus obtained Grignard reagent of 3-vinylphenylmagnesium bromide, a solution of 122.6 g (1.02 mole) of acetophenone in 500 ml of dried tetrahydrofuran was dropped little by little over 2 hours. The reaction temperature was maintained at 75.degree. to 80.degree. C. and, after the dropping, the stirring was continued for further 1 hour as it stands. The reaction mixture was then poured into 3 liter of an aqueous solution of 75 g of ammonium chloride and it was left to stand still for 20 hours and an oily layer was recovered to obtain 1-(3-vinylphenyl)-1-phenylethyl alcohol in a yield of 89% (acetophenone basis) by distilling off the tetrahydrofuran.
To a 300 ml three-neck flask with a distillation column and a dropping funnel was added 81 g of potassium hydrogensulfate and the pressure was reduced to 15 to 20 mm Hg. The obtained alcohol was then dropped into the flask little by little over 2 hours. The water produced by dehydration and oily components were recovered from the top of the distillation column and 1-(3-vinylphenyl)-1-phenylethylene was obtained in a yield of 100% (on the basis of raw material alcohol) from the oily layer by a separatory funnel. The dehydration reaction was carried out at a temperature of 200.degree. to 250.degree. c.