(en)1. A PROCESS FOR THE PREPARATION OF TRANS-2-HEXENAL, WHICH CONSISTS ESSENTIALLY OF TREATING AT 50-180*C. A WATER SUSPENSIPN OF CYCLOHEXYL HYDROPEROXIDE WITH AN AQUEOUS SOLUTION OF PALLADIUM CHLORIDE.

1.ApplicationNumber: US-16663671-A
1.PublishNumber: US-3839457-A
2.Date Publish: 19741001
3.Inventor: JOUFFRET M,FR

4.Inventor Harmonized: JOUFFRET M()

5.Country: US
6.Claims:
(en)1. A PROCESS FOR THE PREPARATION OF TRANS-2-HEXENAL, WHICH CONSISTS ESSENTIALLY OF TREATING AT 50-180*C. A WATER SUSPENSIPN OF CYCLOHEXYL HYDROPEROXIDE WITH AN AQUEOUS SOLUTION OF PALLADIUM CHLORIDE.

7.Description:
(en)United States Patent 3,839,457 PROCESS FOR THE PREPARATION OF Z-HEXENAL Michel .louirret, Frauchevillle-le-Bas, France, assiguor to Rhone-Poulenc S.A., Paris, France No Drawing. Filed July 27, 1971, Ser. No. 166,636 Claims priority, application France, July 28, 1970, 7027793 Int. Cl. C07c 47/20 US. Cl. 260-601 R 7 Claims ABSTRACT OF THE DISCLOSURE Trans-Z-hexenal is obtained by treating cyclohexyl hydroperoxide in the liquid phase with an aqueous solution of a palladium derivative e.g. PdCl 2H O'. An aqueous suspension of hydroperoxide, optionally with a Water immiscible organic solvent such as cyclohexane, may be heated at 50180 C. with the palladium derivative.
The present invention relates to a new process for producing trans-Z-hexenal. 2-Hexenal, has been prepared previously by oxidation of 2-hexen-1-ol with chromic acid [Delaby and Guillot-Allegre-C.R. Acad. Sc. 1468 (1931)] and by dehydration of 2-hexene-1,4-diol [Prevost-Bull. Soc. Chim. Fr. 11 224 (1944)].
The present invention provides a particularly simple process for preparing trans-Z-hexenal which is very suitable for exploitation on an industrial scale.
The present invention provides a process for the preparation of trans-'2-hexenal, wherein cyclohexyl hydroperoxide is treated in the liquid phase with an aqueous solution of a palladium derivative. The term palladium derivative is applied to the product which is made into a solution.
Cyclohexyl hydroperoxide can be obtained from cyclohexanol or by oxidation of cyclohexane in the liquid phase, without a catalyst, by means of .a gas containing molecular oxygen, optionally in the presence of agents capable of complexing metal ions, for example, as described in French Patent Specification Nos. 1,404,723, and 1,491,518. The hydroperoxide can be purified by known method such as conversion to the sodium salt and treatment of the sodium salt with carbon dioxide.
The hydroperoxide can be used in the form of a suspension in water. For technological and economic reasons, it is advantageous to use amounts of water such that the proportion by weight of hydroperoxide in the suspension is between 2% and 50%, and preferably between 5 and 30%.
The process can also be carried out in the presence of an organic solvent for the hydroperoxide, preferably a solvent which is immiscible with water. This solvent can, for example, be a linear ether, an ester such as a lower alkyl alkylcarboxylate or arylcarboxylate, or a hydrocarbon. Because of their easy availability, it is preferred to use as solvent alkanes or alkenes having from 6 to 20 carbon atoms, cycloalkanes or cycloalkenes having from 5 to 16 carbon atoms in the ring and optionally substituted by alkyl radicals having from 1 to 4 carbon atoms, or benzene or monosubstituted or polysubstituted benzenes where the substituent(s) is chlorine or fluorine, alkyl of 1 to 4 carbon atoms, alkoxy of 1 to 4 carbon atoms, nitro or nitrile, a phenyl radical which itself may be substituted by alkyl or alkoxy of 1 to 4 carbon atoms or by nitro or nitrile. It is also possible to use aromatic hydrocarbons with partially condensed or wholly hydrogenated rings, such as tetralin or decalin. For the reasons given above, it is advantageous to use amounts of water and of organic solvent such that the proportion by weight of hydroperoxide in the mixture used for the reaction is between the ice values given above. If an organic solvent, such as defined above, is used, the weight of water should be at least of the order of 1% relative to the weight of the organic solution, which can be saturated with water if appropriate; the preferred weights, expressed in the same way, are between 5% and 20%.
As palladium catalyst the chlorine, optionally in the hydrated form, can be used with advantage. The amounts of catalyst are generally chosen in such a way that they introduce from 1 to 20 gram atoms of elemental metal per mols of hydroperoxide involved. The preferred amounts, again relative to 100 mols of hydroperoxide, are between 5 and 15 gram atoms of elemental palladium.
The process of the invention may be put into practice by mixing the hydroperoxide, the water and, where relevant, the organic solvent, at ordinary temperature, and then adding the catalyst; thereafter the mixture is heated to the chosen temperature, which is generally between 50 and 180 C. and preferably between 70 and 150 C. In an alternative procedure, the hydroperoxide, optionally in solution, can be introduced into the mixture of the other constituents previously heated to the chosen temperature. If the temperature employed is above the boiling point of the mixture, the reaction can be carried out in an apparatus which is under pressure. The mixture can be kept in the liquid phase, if appropriate, by introducing an inert gas such as nitrogen or argon. At the end of the reaction, the duration of which is of the order of several hours, the trans-2-hexenal formed can be isolated from the residual mixture by applying the usual methods, for example by fractional distillation.
The pharmacological, fungicidal, anti-microbial and bronzing properties of trans-Z-hexenal make it of great interest in cosmetics. This aldehyde is one of the principles responsible for the greenness in nature; its use is widespread in the field of aroma substances (BedoukianPerfumery and Flavoring Synthetics-Elsevier Publishing Company1967 The following Examples are given to illustrate the invention.
EXAMPLE 1 60 g. of a cyclohexane solution containing 10% by weight of cyclohexyl hydroperoxide are introduced into a 250 cm. autoclave. Thereafter 4.5 g. of water are added, followed by 1.5 g. of an aqueous solution of palladium chloride dihydrate containing 35% by weight of elemental palladium. The autoclave is closed and then heated to C. for 3 hours, while the contents are stirred. After cooling and release of the gas, the residual mixture is decanted and the aqueous phase is extracted with ether. The combined organic phases are distilled, and the ether and cyclohexane removed.
Vapour phase chromatography shows that the residue contains 2.3 g. of 2-hexenal as well as 0.345 g. of cyclohexanol and 0.35 g. of cyclohexanone. N.M.R. examina tion of a sample shows that the 2-hexenal is of trans structure.
EXAMPLE 2 A mixture of 585 g. of cyclohexane, 30.4 g. of
Pd'Cl -2NaCl and 90 g. of Water is boiled (77 C.) and a solution prepared from 273 g. of cyclohexane and 125 g. of cyclohexyl hydroperoxide is then gradually introduced over the course of 1 hour 40 minutes. The mixture is thereafter boiled for 2 hours 40 minutes.
After cooling, the mixture is filtered and decanted, and the organic layer is twice washed, using 60 g. of water each time. The organic phase is gradually distilled under reduced pressure, the cyclohexane is removed first and a fraction then collected which contains 53 g. of trans-2 hexenal, 16 g. of cyclohexanone and 8.8 g. of cyclohexanol.
The trans-2-hexenal is thereafter isolated from the mixture by fractional distillation under 100 mm. of mercury, using a rotating strip column.
I claim:
1. A process for the preparation of trans-Z-hexenal, which consists essentially of treating at 50180 C.
a water suspension of cyclohexyl hydroperoxide with an aqueous solution of palladium chloride.
2. A process according to claim 1 wherein said water suspension comprises 250% by weight of cyclohexyl hydroperoxide.
3. A process according to claim 1 wherein the palladium chloride is palladium chloride dihydrate.
4. A process according to claim 1 wherein the treatment is carried out in the presence of an amount of palladium chloride containing 1-20 gram atoms palladium per 100 moles of hydroperoxide.
5. A process for the preparation of trans-Z-hexenal which consists essentially of treating an organic solvent solution of cyclohexyl hydroperoxide at 50 to 180 C.
with an aqueous solution of palladium chloride,
the organic solvent for the hydroperoxide being immiscible with water so that two liquid phases are formed; said solvent being selected from the group consisting of alkanes and alkenes having from 6 to 20 carbon atoms, cycloalkanes and cycloalkenes having from 5 to 16 carbon atoms in the ring and optionally substituted by alkyl radicals having from 1 to 4 carbon atoms, benzene, mono-substituted and polysubstituted benzenes where the substituent(s) is chlorine or fluorine, alkyl of 1 to 4 carbon atoms, alkoxy of 1 to 4 carbon atoms, nitro or nitrile, a phenyl radical which itself may be substituted by alkyl or alkoxy of 1 to 4 carbon atoms or by nitro or nitrile; tetralin and decalin and recovering trans-Z-hexenal from the organic phase.
6. A process according to claim 5 wherein the organic solvent is cyclohexane.
7. A process according to claim 5 wherein the treatment is carried out in the presence of a mixture of the organic solvent and water containing 520% by weight of water relative to the organic solution.
290,978 6/1965 Netherlands 260-610 393,312 10/1965 Switzerland 260610 BERNARD HELFIN, Primary Examiner D. B. SPRINGER, Assistant Examiner