WO2006120639A2 - Catalytic scriabine reaction - Google Patents
Catalytic scriabine reaction Download PDFInfo
- Publication number
- WO2006120639A2 WO2006120639A2 PCT/IB2006/051451 IB2006051451W WO2006120639A2 WO 2006120639 A2 WO2006120639 A2 WO 2006120639A2 IB 2006051451 W IB2006051451 W IB 2006051451W WO 2006120639 A2 WO2006120639 A2 WO 2006120639A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- formula
- group
- compound
- optionally substituted
- diacetate
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/77—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D307/78—Benzo [b] furans; Hydrogenated benzo [b] furans
- C07D307/79—Benzo [b] furans; Hydrogenated benzo [b] furans with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to carbon atoms of the hetero ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/28—Preparation of carboxylic acid esters by modifying the hydroxylic moiety of the ester, such modification not being an introduction of an ester group
- C07C67/293—Preparation of carboxylic acid esters by modifying the hydroxylic moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/77—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D307/91—Dibenzofurans; Hydrogenated dibenzofurans
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D317/00—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
- C07D317/08—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
- C07D317/44—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D317/46—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 ortho- or peri-condensed with carbocyclic rings or ring systems condensed with one six-membered ring
- C07D317/48—Methylenedioxybenzenes or hydrogenated methylenedioxybenzenes, unsubstituted on the hetero ring
- C07D317/50—Methylenedioxybenzenes or hydrogenated methylenedioxybenzenes, unsubstituted on the hetero ring with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to atoms of the carbocyclic ring
- C07D317/54—Radicals substituted by oxygen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/16—Systems containing only non-condensed rings with a six-membered ring the ring being unsaturated
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2602/00—Systems containing two condensed rings
- C07C2602/02—Systems containing two condensed rings the rings having only two atoms in common
- C07C2602/04—One of the condensed rings being a six-membered aromatic ring
- C07C2602/08—One of the condensed rings being a six-membered aromatic ring the other ring being five-membered, e.g. indane
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2602/00—Systems containing two condensed rings
- C07C2602/02—Systems containing two condensed rings the rings having only two atoms in common
- C07C2602/04—One of the condensed rings being a six-membered aromatic ring
- C07C2602/10—One of the condensed rings being a six-membered aromatic ring the other ring being six-membered, e.g. tetraline
Definitions
- the present invention relates to the field of organic synthesis. More particularly it provides a process for making aromatic non-conjugated enol esters or enol ethers from an aromatic compound or moiety and a protected enal compound or moiety, such as an acetal or an acylal. The reaction is promoted by the use of some metal derivatives.
- the Scriabine reaction consists of the reaction between an aromatic compound and an enal or the corresponding acylal (see I. Scriabine in Bull. Soc. Chem.Fr., 1961, 1194). This reaction provides an access to the formation of dihydrocinnamic aldehyde derivatives. To the best of our knowledge, all the methods and examples reported in the literature concerning this reaction are at least steochiometric in an Al salt or in TiCl 4 . For instance one may cite Aguillar et al. in Synthetic Comm. 2004, 2719.
- the present invention provides a process for making a compound of the formula
- each R 1 represents, taken separately, a hydrogen or halogen atom or a C 1 -C 6 alkyl, alkoxy or amino group; or the two R 1 , when taken together, represent a C 3 -C 10 alkanediyl or alkenediyl group optionally substituted and optionally comprising one or two oxygen, sulfur or nitrogen atoms;
- R 2 or R 3 represents, taken separately, a hydrogen atom or a C 1 -C 6 alkyl group; R 2 and R 3 , taken together, may represent a C 3 -C 10 alkanediyl or alkenediyl group optionally substituted;
- R 4 represents a C 1 -C 7 alkyl or fluorinated alkyl group, a C 7 -C 10 alkylaromatic optionally substituted, a C 1 -C 7 acyl group, or a -COCOOH or -COCH 2 COOH group; and R 5 represents a C 2 -C 9 alkanediyl or alkenediyl group optionally substituted; comprising the coupling of a compound of formula (II) with a compound of formula (III)
- R 1 to R 3 have the meaning indicated in formula (I) and each R 6 , taken separately, represents a C 1 -C 7 alkyl or fluorinated alkyl group, a C 7 -C 10 alkylaromatic optionally substituted, a C 1 -C 7 acyl group, or the R 6 , taken together, represent a COCO or COCH 2 CO group; or, respectively, the cyclisation of a compound of formula
- R 1 and R 3 have the meaning indicated in formula (I), R 6 has the meaning indicated in formula (III), and R 5 has the meaning indicated in formula (F); said processes being characterized in that it is carried out in the presence of a catalytic amount of at least one catalyst selected from the group consisting of
- M representing a transition metal selected from the group consisting of Fe, Co, Ni, Cu and Zn, X representing a mono-anion and n is an integer from 1 to 3;
- Y represents a fluoride or a phenyl group optionally substituted, and anyone of its adducts with a C 2 -C 10 ether or a C 1 -C 8 carboxylic acid.
- R 1 to R 6 Possible substituents of R 1 to R 6 are one, two or three halogen atoms or OR a , NR a 2 or R a groups, in which R a is a hydrogen atom or a C 1 to C 10 cyclic, linear or branched alkyl or alkenyl group, preferably a C 1 to C 4 linear or branched alkyl or alkenyl group.
- Possible substituents of Y are one to five groups such as halide atoms or methyl or CF 3 groups.
- the compound of formula (I), or (F) can be in the form of a mixture of isomers.
- the compound of formula (II) is methyl-benzene, then the compound (I) obtained can be in the form of a mixture of the ortho, or meta, and para isomers.
- the invention provides a process for making a compound of formula (I) or (F) wherein R 4 represents a C 1 -C 7 alkyl group, a benzyl group optionally substituted or a C 1 -C 7 acyl group.
- R 2 or R 3 may represent, taken separately, a hydrogen atom or a C 1 -C 4 alkyl group; R 2 and R 3 , taken together, may represent a C 3 , C 4 or C 10 alkanediyl or alkenediyl group optionally substituted.
- each R 1 may represent, taken separately, a hydrogen or halogen atom or a C 1 -C 4 alkyl or alkoxy group; or the two R 1 , when taken together, represent a C 3 -C 5 alkanediyl or alkenediyl group optionally substituted and optionally comprising one or two oxygen, sulfur or nitrogen atoms. According to a further embodiment, one, or the two, R 1 are not a hydrogen atom.
- R 5 may also represent a C 2 -C 3 alkanediyl or alkenediyl group optionally substituted.
- the starting material are the corresponding compounds of formula (II) and (III), or the corresponding compound of formula (IV).
- the invention provides a process for making a compound of formula (I) by the reaction of a compound of formula (II) with a compound of formula (III).
- compound of formula (II) one may cite the following: benzene optionally substituted by one or two C 1 -C 4 alkyl groups, 1,3-benzodioxole or indane optionally substituted by one or two C 1 -C 4 alkyl groups, and in particular 1,1- dimethyl indane.
- compound of formula (III) one may cite the following: acrolein diethyl acetal, acrolein diacetate, methacrolein diacetate, crotonaldehyde diacetate, tiglyl diacetate, cyclohexenyl carbaldehyde diacetate.
- the invention process is carried out in the presence of at least one catalyst which is a salt of formula MX n or a compound of formula BY 3 and adducts thereof.
- Said catalyst can be in the anhydrous form or also in the hydrate form, except for those acids which are unstable in the presence of water.
- the anhydrous form is preferred.
- the use of only one compound of formula MX n as catalysts is also preferred.
- the catalyst is selected from the group consisting of BY 3 and adducts thereof, FeX 3 , CoX 2 , NiX 2 , ZnX 2 , CuX 2 and CuX.
- the catalyst is selected from the group consisting of BY 3 and its adducts above mentioned, FeX 3 , NiX 2 , ZnX 2 , and CuX 2 are particularly useful. Yet, more particularly, the catalyst may be a selected amongst BY 3 and its adducts above mentioned, FeX 3 , and ZnX 2 .
- BY 3 can be used alone or in the form of one of its adducts with an ether or a carboxylic acid. Specific examples are the adducts of BF 3 with Et 2 O, Bu 2 O or AcOH.
- X is a mono-anion selected from the group consisting of acetylacetonate optionally substituted, Cl “ , Br “ , C 1-9 carboxylate, a C 1-10 sulphonate, ClO 4 " , BF 4 -, PF 6 -, SbCl 6 ", AsCl 6 “, SbF 6 “, AsF 6 “, BR 7 4 " , wherein R 7 is a phenyl group optionally substituted by one to five groups such as halide atoms or methyl or CF 3 groups, or a R 8 SO 3 " , wherein R 8 is a chlorine or fluoride atom.
- X can be selected from the group consisting of Cl " , Br " and
- Y is F or C 6 H 5 .
- the catalyst is BF 3 and its adducts with AcOH, FeCl 3 , ZnBr 2 or ZnCl 2 .
- the catalyst can be added to the reaction medium in a large range of concentrations.
- concentrations ranging from 0.001 to 0.30 molar equivalents, relative to the molar amount of the starting compound (II) or (IV).
- the catalyst concentrations will be comprised between 0.005 and 0.15 molar equivalents.
- the optimum concentration of catalyst will depend on the nature of the catalyst and on the desired reaction time.
- catalyst concentrations ranging from 0.1 to 0.30 molar equivalents, relative to the molar amount of the starting compound (III).
- the catalyst concentrations will be comprised between 0.01 and 0.10 molar equivalents.
- catalyst amount we mean here any amount which allow the formation of the desired compound with a molar yield which exceeds the molar equivalents of catalyst added to the reaction mixture.
- the temperature at which the invention's process can be carried out is typically between 0°C and 180°C, more preferably in the range of between 15°C and 100°C.
- a person skilled in the art is also able to select the preferred temperature as a function of the melting and boiling point of the starting and final products.
- a person skilled in the art is also able to select the preferred temperature as a function of the melting and boiling point of the starting and final products as well as of the solvent.
- the process of the invention can be carried out in the presence or in the absence of solvent.
- the presence of a solvent is mandatory only in the case in which the starting compound is a solid compound under the reaction conditions.
- the process is advantageously carried out in the presence of a solvent.
- a solvent is anhydrous or does not contain more than 1% w/w water.
- Non-limiting examples of such a solvent are C 4 -C 8 ethers, C 3 -C 6 esters, C 3 -C 6 amides, C 6 -C 9 aromatic solvents, C 5 -C 7 linear or branched or cyclic hydrocarbons, C 1 -C 2 chlorinated solvents and mixtures thereof.
- reaction can also be carried out in the presence of a solvent belonging to the family of carboxylic anhydride of formula R 9 C(O)O(O)CR 9 , R 9 representing a C 1 -C 7 alkyl group, a C 7 -C 10 alkylaromatic optionally substituted, a C 1 -C 7 acyl group, optionally containing the corresponding carboxylic acid R 9 COOH.
- R 9 belonging to the family of carboxylic anhydride of formula R 9 C(O)O(O)CR 9
- R 9 representing a C 1 -C 7 alkyl group, a C 7 -C 10 alkylaromatic optionally substituted, a C 1 -C 7 acyl group, optionally containing the corresponding carboxylic acid R 9 COOH.
- R 9 belonging to the family of carboxylic anhydride of formula R 9 C(O)O(O)CR 9
- R 9 representing a C 1 -C 7 alkyl group, a C 7 -C 10 alky
- the compound of formula (III) or (IV) can be made and isolated according to any prior art method.
- compound (III) or (IV) can be also generated in situ, i.e. in the reaction medium just before its use, according to any know prior art method.
- the compound of formula (III) or (IV) is made or generated by a method using the corresponding enal as starting material.
- Another object of the present invention is an invention's process, as defined above, further comprising the step of generating in situ the compound of formula (III) or (IV) starting from the corresponding enal of formula (V) or (V) respectively
- R 1 , R 2 , R 3 and R 5 have the same meaning indicated above.
- a process comprising the in situ generation of the compound of formula (III) or (F) is particularly useful when said compound (III) or (F) is an acetal or an acylal, the latter being a geminal dicarboxylate.
- another object of the present invention is a process for making a compound of formula (I) or (F), as defined above, comprising the step of reacting, in the presence of a catalyst as defined above, an enal of formula (V) or (V), as defined above, with a carboxylic anhydride of formula R 9 C(O)O(O)CR 9 , wherein R 9 has the meaning indicated above.
- the aqueous phase was re- extracted with ethyl acetate (150 ml).
- the combined organic phases were washed with saturated aqueous NaHCO 3 solution (100 ml), brine (100 ml), dried over MgSO 4 and the solvents removed in vacuo. Further purification by KugelRohr distillation at 150°C (2.9 x 10 "1 mbar) gave the desired enol acetate as a mixture of isomers (7.2 g, 30%).
- Zinc bromide 50 mg, 0.2 mmol was suspended in a solution of acrolein diacetate (1.6 g, 10 mmol), 2,2 dimethyl dihydrobenzofuran (1.5 g, 10 mmol), in dichloromethane (5 g) and the stirred at ambient temperature for 24 hours. The reaction medium was then diluted with ethyl acetate (25 ml) and the saturated aqueous NaHCO 3 solution (20 ml) was added slowly dropwise. The aqueous phase was re-extracted with ethyl acetate (25 ml).
- BF 3 acetic acid complex (0.2 g, 1 mmol) was added to a stirred solution of 2-methyl indane (13.2 g, 100 mmol) and methacrolein diacetate (8.7 g, 50 mmol) heated at 60°C. The mixture was stirred at 60°C for one hour, then cooled and diluted with ethyl acetate (50 ml), and saturated aqueous NaHCO 3 solution (50 ml) was added slowly dropwise. The aqueous phase was re-extracted with ethyl acetate (50 ml), the combined organic phase was washed with NaHCO 3 (100 ml), dried over MgSO 4 , filtered and the solvents removed in vacuo.
- the aqueous phase was re-extracted with ethyl acetate (50 ml), the combined organic phase was washed with bicarbonate (50 ml) then brine (50 ml), dried over magnesium sulfate, filtered and the solvents removed in vacuo.
- the crude product was purified by Kugelrohr distillation, firstly under moderate vacuum (5-10 mbar) to recover the indane, then under high vacuum (1.0-4.0 x 10 "1 mbar).
- Zinc chloride (0.14 g, 1 mmol, 10 mol%) was added to a stirred solution of 1,3 methylenedioxy benzene (2.4 g, 20 mmol) and methacrolein diacetate (1.72 g, 10 mmol) at ambient temperature. The solution was stirred at ambient temperature for a further 48 hours. The solution was diluted with ethyl acetate (59 ml), and sodium bicarbonate 5% (50 ml), the aqueous phase was re-extracted with ethyl acetate (50 ml), the organic phase was washed with brine (50 ml), dried over magnesium sulfate, filtered and the solvents removed in vacuo.
- Zinc chloride (0.14 g, 1 mmol), was added to a solution of anisole (2.16 g, 20 mmol) and tiglic diacetate (1.86 g, 10 mmol), and the mixture stirred at ambient temperature for 3 hours.
- the solution was diluted with ethyl acetate (25 ml) and saturated sodium bicarbonate (50 ml), the aqueous phase was re-extracted with ethyl acetate (25 ml) the combined organic phases were washed with brine, dried over magnesium sulfate, filtered and the solvents removed in vacuo.
- Acetic anhydride (5 g, 49 mmol) was added to a suspension of FeCl 3 .6H 2 O (1.08 g, 4 mmol) and 2-methyl indane (26.4 g, 200 mmol), after 5 mins crotonaldehyde diacetate (6.88 g, 40 mmol) was added slowly drop wise. The mixture was stirred for a further 7 hours, then poured into brine (50 ml), extracted with ether (100 ml), washed the organic extract with sodium bicarbonate (100 ml), then brine (50 ml), dried over magnesium sulfate, filtered and the solvents removed in vacuo.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Saccharide Compounds (AREA)
- Furan Compounds (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP06744885.2A EP1888502B1 (en) | 2005-05-11 | 2006-05-09 | Catalytic scriabine reaction |
CN2006800151490A CN101171223B (en) | 2005-05-11 | 2006-05-09 | Catalytic scriabine reaction |
JP2008510707A JP5376939B2 (en) | 2005-05-11 | 2006-05-09 | Catalytic scriabin reaction |
ES06744885.2T ES2595498T3 (en) | 2005-05-11 | 2006-05-09 | Catalytic Reaction of Escriabine |
US11/861,078 US7524983B2 (en) | 2005-05-11 | 2007-09-25 | Catalytic scriabine reaction |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IB2005001310 | 2005-05-11 | ||
IBPCT/IB2005/001310 | 2005-05-11 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/861,078 Continuation US7524983B2 (en) | 2005-05-11 | 2007-09-25 | Catalytic scriabine reaction |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2006120639A2 true WO2006120639A2 (en) | 2006-11-16 |
WO2006120639A3 WO2006120639A3 (en) | 2007-03-08 |
Family
ID=37114366
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IB2006/051451 WO2006120639A2 (en) | 2005-05-11 | 2006-05-09 | Catalytic scriabine reaction |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1888502B1 (en) |
JP (1) | JP5376939B2 (en) |
CN (1) | CN101171223B (en) |
ES (1) | ES2595498T3 (en) |
WO (1) | WO2006120639A2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008059841A1 (en) * | 2006-11-13 | 2008-05-22 | Ube Industries, Ltd. | Process for production of 1-acyloxy-3-(3,4- methylenedioxyphenyl)-1-propene compound |
WO2008099882A1 (en) | 2007-02-15 | 2008-08-21 | Ube Industries, Ltd. | 2-methyl-3-(3,4-methylenedioxyphenyl)propanal, and method for production thereof |
WO2008108429A1 (en) | 2007-03-07 | 2008-09-12 | Ube Industries, Ltd. | Method of retaining the quality of 2-methyl-3-(3,4-methylenedioxyphenyl)propanal and process for producing the same |
WO2013001027A1 (en) * | 2011-06-30 | 2013-01-03 | Firmenich Sa | Process for the preparation of beta-santalol |
WO2022018054A1 (en) | 2020-07-24 | 2022-01-27 | Firmenich Sa | Process for preparing indene acryladehyde derivatives |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2726447B1 (en) * | 2011-06-30 | 2015-08-12 | Firmenich SA | Process for the preparation of beta-santalol |
US11312873B2 (en) * | 2019-09-04 | 2022-04-26 | Eastman Chemical Company | Aromatic enol ether paint additives |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61161241A (en) | 1985-01-08 | 1986-07-21 | Mitsubishi Rayon Co Ltd | Production of aldehyde derivative |
EP1574509A1 (en) | 2002-12-18 | 2005-09-14 | Ube Industries, Ltd. | Process for the production of 1-acetoxy-3-(substituted phenyl)propenes |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3548006A (en) * | 1963-03-15 | 1970-12-15 | Rhone Poulenc Sa | Aldehydes useful in perfumery |
JPS61151152A (en) * | 1984-12-24 | 1986-07-09 | Mitsubishi Rayon Co Ltd | Production of alkenylidene diacetate |
DE69516036T2 (en) * | 1994-05-31 | 2000-12-21 | Firmenich S.A., Genf/Geneve | Aromatic compounds and their use in perfumery |
-
2006
- 2006-05-09 ES ES06744885.2T patent/ES2595498T3/en active Active
- 2006-05-09 WO PCT/IB2006/051451 patent/WO2006120639A2/en not_active Application Discontinuation
- 2006-05-09 CN CN2006800151490A patent/CN101171223B/en active Active
- 2006-05-09 JP JP2008510707A patent/JP5376939B2/en active Active
- 2006-05-09 EP EP06744885.2A patent/EP1888502B1/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61161241A (en) | 1985-01-08 | 1986-07-21 | Mitsubishi Rayon Co Ltd | Production of aldehyde derivative |
EP1574509A1 (en) | 2002-12-18 | 2005-09-14 | Ube Industries, Ltd. | Process for the production of 1-acetoxy-3-(substituted phenyl)propenes |
Non-Patent Citations (1)
Title |
---|
I. SCRIABINE, BULL. SOC. CHEM.FR., 1961, pages 1194 |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008059841A1 (en) * | 2006-11-13 | 2008-05-22 | Ube Industries, Ltd. | Process for production of 1-acyloxy-3-(3,4- methylenedioxyphenyl)-1-propene compound |
WO2008099882A1 (en) | 2007-02-15 | 2008-08-21 | Ube Industries, Ltd. | 2-methyl-3-(3,4-methylenedioxyphenyl)propanal, and method for production thereof |
US8168809B2 (en) | 2007-02-15 | 2012-05-01 | Ube Industries, Ltd. | 2-methyl-3-(3,4-methylenedioxyphenyl)propanal, and method for production thereof |
EP2562173A1 (en) | 2007-02-15 | 2013-02-27 | Ube Industries, Ltd. | 2-methyl-3-(3,4.methylenedioxyphenyl) propanal, and method for production thereof |
US8450508B2 (en) | 2007-03-07 | 2013-05-28 | Ube Industries, Ltd. | Method of retaining the quality of 2-methyl-3-(3,4-methylenedioxyphenyl)propanal and process for producing the same |
WO2008108429A1 (en) | 2007-03-07 | 2008-09-12 | Ube Industries, Ltd. | Method of retaining the quality of 2-methyl-3-(3,4-methylenedioxyphenyl)propanal and process for producing the same |
US8039649B2 (en) | 2007-03-07 | 2011-10-18 | Ube Industries, Ltd. | Method of retaining the quality of 2-methyl-3-(3,4-methylenedioxyphenyl)propanal and process for producing the same |
US8344166B2 (en) | 2007-03-07 | 2013-01-01 | Ube Industries, Ltd. | Method of retaining the quality of 2-methyl-3-(3,4-methylenedioxyphenyl) propanal and process for producing the same |
WO2013001027A1 (en) * | 2011-06-30 | 2013-01-03 | Firmenich Sa | Process for the preparation of beta-santalol |
CN103619789A (en) * | 2011-06-30 | 2014-03-05 | 弗门尼舍有限公司 | Process for the preparation of beta-santalol |
US9156770B2 (en) | 2011-06-30 | 2015-10-13 | Firmenich Sa | Process for the preparation of beta-santalol |
US9212112B1 (en) | 2011-06-30 | 2015-12-15 | Firmenich Sa | Process for the preparation of beta-santalol |
WO2022018054A1 (en) | 2020-07-24 | 2022-01-27 | Firmenich Sa | Process for preparing indene acryladehyde derivatives |
Also Published As
Publication number | Publication date |
---|---|
WO2006120639A3 (en) | 2007-03-08 |
CN101171223B (en) | 2012-07-04 |
ES2595498T3 (en) | 2016-12-30 |
JP5376939B2 (en) | 2013-12-25 |
EP1888502B1 (en) | 2016-07-13 |
EP1888502A2 (en) | 2008-02-20 |
CN101171223A (en) | 2008-04-30 |
JP2008544955A (en) | 2008-12-11 |
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