WO1990009975A1 - Oxydation d'aldehydes - Google Patents
Oxydation d'aldehydes Download PDFInfo
- Publication number
- WO1990009975A1 WO1990009975A1 PCT/GB1990/000313 GB9000313W WO9009975A1 WO 1990009975 A1 WO1990009975 A1 WO 1990009975A1 GB 9000313 W GB9000313 W GB 9000313W WO 9009975 A1 WO9009975 A1 WO 9009975A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- aldehyde
- substituent
- process according
- carboxylic acid
- aromatic
- Prior art date
Links
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 16
- 230000003647 oxidation Effects 0.000 title claims abstract description 15
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 title 1
- 150000001299 aldehydes Chemical class 0.000 claims abstract description 28
- 238000000034 method Methods 0.000 claims abstract description 25
- 125000001424 substituent group Chemical group 0.000 claims abstract description 20
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims abstract description 16
- 150000003934 aromatic aldehydes Chemical class 0.000 claims abstract description 8
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000001257 hydrogen Substances 0.000 claims abstract description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 6
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims abstract description 6
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 3
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 3
- 238000006243 chemical reaction Methods 0.000 claims description 26
- 239000000758 substrate Substances 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 5
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims description 5
- -1 polycyclic arene Chemical class 0.000 claims description 5
- 125000004001 thioalkyl group Chemical group 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- IBDSNZLUHYKHQP-UHFFFAOYSA-N sodium;3-oxidodioxaborirane;tetrahydrate Chemical compound O.O.O.O.[Na+].[O-]B1OO1 IBDSNZLUHYKHQP-UHFFFAOYSA-N 0.000 claims description 3
- XSVSPKKXQGNHMD-UHFFFAOYSA-N 5-bromo-3-methyl-1,2-thiazole Chemical compound CC=1C=C(Br)SN=1 XSVSPKKXQGNHMD-UHFFFAOYSA-N 0.000 claims description 2
- 125000001931 aliphatic group Chemical group 0.000 claims description 2
- 125000002648 azanetriyl group Chemical group *N(*)* 0.000 claims description 2
- 150000003935 benzaldehydes Chemical class 0.000 claims description 2
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 claims description 2
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 claims 3
- 239000007858 starting material Substances 0.000 claims 3
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims 2
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 claims 2
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 claims 1
- 125000002619 bicyclic group Chemical group 0.000 claims 1
- 125000001475 halogen functional group Chemical group 0.000 claims 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims 1
- 239000000047 product Substances 0.000 description 11
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000012429 reaction media Substances 0.000 description 5
- VFZRZRDOXPRTSC-UHFFFAOYSA-N 3,5-Dimethoxybenzaldehyde Chemical compound COC1=CC(OC)=CC(C=O)=C1 VFZRZRDOXPRTSC-UHFFFAOYSA-N 0.000 description 4
- 229960000583 acetic acid Drugs 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 4
- 239000007800 oxidant agent Substances 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- 235000010233 benzoic acid Nutrition 0.000 description 3
- 239000012043 crude product Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N Butyraldehyde Chemical compound CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 150000001559 benzoic acids Chemical class 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 150000001735 carboxylic acids Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000012362 glacial acetic acid Substances 0.000 description 2
- 125000005843 halogen group Chemical group 0.000 description 2
- FXHGMKSSBGDXIY-UHFFFAOYSA-N heptanal Chemical compound CCCCCCC=O FXHGMKSSBGDXIY-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- GYHFUZHODSMOHU-UHFFFAOYSA-N nonanal Chemical group CCCCCCCCC=O GYHFUZHODSMOHU-UHFFFAOYSA-N 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- DTUQWGWMVIHBKE-UHFFFAOYSA-N phenylacetaldehyde Chemical compound O=CCC1=CC=CC=C1 DTUQWGWMVIHBKE-UHFFFAOYSA-N 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- 229960001922 sodium perborate Drugs 0.000 description 2
- 239000012418 sodium perborate tetrahydrate Substances 0.000 description 2
- YKLJGMBLPUQQOI-UHFFFAOYSA-M sodium;oxidooxy(oxo)borane Chemical compound [Na+].[O-]OB=O YKLJGMBLPUQQOI-UHFFFAOYSA-M 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000004809 thin layer chromatography Methods 0.000 description 2
- FODBVCSYJKNBLO-UHFFFAOYSA-N 2,3-dimethoxybenzoic acid Chemical compound COC1=CC=CC(C(O)=O)=C1OC FODBVCSYJKNBLO-UHFFFAOYSA-N 0.000 description 1
- PIKNVEVCWAAOMJ-UHFFFAOYSA-N 3-fluorobenzaldehyde Chemical compound FC1=CC=CC(C=O)=C1 PIKNVEVCWAAOMJ-UHFFFAOYSA-N 0.000 description 1
- AVPYQKSLYISFPO-UHFFFAOYSA-N 4-chlorobenzaldehyde Chemical compound ClC1=CC=C(C=O)C=C1 AVPYQKSLYISFPO-UHFFFAOYSA-N 0.000 description 1
- 239000005711 Benzoic acid Substances 0.000 description 1
- ROFVEXUMMXZLPA-UHFFFAOYSA-N Bipyridyl Chemical group N1=CC=CC=C1C1=CC=CC=N1 ROFVEXUMMXZLPA-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 238000007027 Dakin phenol oxidation reaction Methods 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- DGEZNRSVGBDHLK-UHFFFAOYSA-N [1,10]phenanthroline Chemical compound C1=CN=C2C3=NC=CC=C3C=CC2=C1 DGEZNRSVGBDHLK-UHFFFAOYSA-N 0.000 description 1
- 125000003172 aldehyde group Chemical group 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- 150000001558 benzoic acid derivatives Chemical class 0.000 description 1
- VBQDSLGFSUGBBE-UHFFFAOYSA-N benzyl(triethyl)azanium Chemical compound CC[N+](CC)(CC)CC1=CC=CC=C1 VBQDSLGFSUGBBE-UHFFFAOYSA-N 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000001246 bromo group Chemical group Br* 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 125000001153 fluoro group Chemical group F* 0.000 description 1
- LHGVFZTZFXWLCP-UHFFFAOYSA-N guaiacol Chemical compound COC1=CC=CC=C1O LHGVFZTZFXWLCP-UHFFFAOYSA-N 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 125000002346 iodo group Chemical group I* 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- OVWYEQOVUDKZNU-UHFFFAOYSA-N m-tolualdehyde Chemical compound CC1=CC=CC(C=O)=C1 OVWYEQOVUDKZNU-UHFFFAOYSA-N 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229940100595 phenylacetaldehyde Drugs 0.000 description 1
- 125000003367 polycyclic group Polymers 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000011027 product recovery Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000010183 spectrum analysis Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C255/00—Carboxylic acid nitriles
- C07C255/49—Carboxylic acid nitriles having cyano groups bound to carbon atoms of six-membered aromatic rings of a carbon skeleton
- C07C255/57—Carboxylic acid nitriles having cyano groups bound to carbon atoms of six-membered aromatic rings of a carbon skeleton containing cyano groups and carboxyl groups, other than cyano groups, bound to the carbon skeleton
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C201/00—Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
- C07C201/06—Preparation of nitro compounds
- C07C201/12—Preparation of nitro compounds by reactions not involving the formation of nitro groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C253/00—Preparation of carboxylic acid nitriles
- C07C253/30—Preparation of carboxylic acid nitriles by reactions not involving the formation of cyano groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
- C07C319/14—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides
- C07C319/20—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides by reactions not involving the formation of sulfide groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/06—Systems containing only non-condensed rings with a five-membered ring
- C07C2601/10—Systems containing only non-condensed rings with a five-membered ring the ring being unsaturated
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/18—Systems containing only non-condensed rings with a ring being at least seven-membered
Definitions
- the present invention relates to the oxidation of aldehydes, and more specifically to the oxidation of aromatic aldehydes to the corresponding carboxylic acids
- oxidising systems that were not only widely available, storage stable, easy to handle and relatively cheap, but would also perform the desired reaction under mild conditions.
- oxidants such as permanganate or dichro ate may be employed, but they inevitably introduce toxic materials, thereby creating waste disposal problems.
- n represents an interger from 1 to 3
- the or each X represents hydrogen or an electron-withdrawing substituent or a mildly electron-donating substituent that is ortho, meta or para to the aldehyde substituent or a strongly electron-donating substituent that is meta to the aldehyde substituent, provided that at least one ortho position is occupied by hydrogen, is brought into contact with an alkali metal perborate and acetic acid at a mild temperature and permitted to react until at least a proportion of the aldehyde has been oxidised to the corresponding aromatic carboxylic acid.
- the substituent X it will be recognised, conveniently can be chosen from a very wide range of substituents, thereby demonstrating the inherent usefulness and widespread applicability of the instant invention process.
- it can be chosen from halo, aldehyde, nitrilo, carboxylic acid, nitro, thioalkyl, alkyl or alkoxy substituents.
- the halo group can be fluoro, chloro, bromo or iodo group, and the alkyl or thioalkyl preferably contains only a small number of carbon atoms.
- the substituent can also comprise a nitrogen hetero-atom within the aromatic nucleus or in a yet further variation the benzene nucleus can be replaced by a di or poly-cyclic aromatic nucleus in which the aldehyde substituent is located at the 2 carbon atom.
- present invention encompasses the oxidation of those aromatic aldehydes that are substituted by a plurality of non-aldehyde substituents, such as two or three.
- a plurality of such substituents each can each be the same as or different from the other or others. It is most advantageous to so array them as to minimise or eliminate steric hindrance effects.
- Suitable examples include di-halo benzaldehydes and 3,5-dimethoxy benzaldehyde.
- the present invention process relates specifically to compounds in which the aldehyde group is a direct and immediate substituent of the aromatic nucleus. It does not extend to the oxidation of saturated aliphatic aldehydes, demonstrated by n-butanal and n-heptanal, or to aromatic compounds in which one or more aliphatic carbons are interposed between the nucleus and the aldehyde, such as phenylacetaldehyde or 2,2-diphenyl cetaldehyde.
- the alkali perborate is particularly conveniently a sodium perborate on account of the bulk availability and excellent storage and handling properties of the two industrially available products sodium perborate monohydrate and sodium perborate tetrahydrate, which have respectively the empirical formulae NaB ⁇ 3.H 2 0 and aB ⁇ 3.4H 2 0, though these do not properly represent the structure of the compounds.
- a particularly safe way comprises introducing it progressively, such as in small portions or continuously during an introductory period, either at or below the desired reaction temperature.
- the invention reaction conditions permit the oxidation of the aldehyde to be effected using only a small excess of perborate beyond the stoichiometric amount of 1 mole per mole of aldehyde.
- a mole ratio for perborateraldehyde selected in the range of from 1:1 to 2:1 and particularly from 1.1:1 to 1.5:1.
- the reaction medium particularly conveniently comprises glacial acetic acid.
- concentration of substrate in the reaction medium can be selected within a very wide range, for example from 0.1M to a saturated solution.
- concentration of substrate in the reaction medium can be selected within a very wide range, for example from 0.1M to a saturated solution.
- concentration of substrate in the reaction medium can be selected within a very wide range, for example from 0.1M to a saturated solution.
- concentration of substrate in the reaction medium can be selected within a very wide range, for example from 0.1M to a saturated solution.
- millid temperature in the context of the present reaction is meant that there is no need to maintain a high temperature during the reaction or even approach closely reflux temperature for the medium. In many instances, it is convenient to employ a temperature that is above ambient, and preferably above 40 & C, up to about 70°C. Very effective oxidations have been achieved in the region of or around 45 to 50°C throughout the reaction period.
- the precise mechanism for the present invention is open to discussion at present. It is speculated that there may be some mode or modes of interaction between the perborate oxidant and the reaction medium which can result in the generation in situ of one or more active species that is or are resposible for the effective oxidation reaction. It will be recognised, though, that the present invention stands by virtue of its demonstrated results and not by the truth or otherwise of any particular point of speculation.
- the total reaction period will usually be determined in practice by taking into account the reaction temperature and the substrate and will often include a period during which perborate is introduced and a subsequent period in which the reaction is allowed to progress.
- the perborate introduction period is often chosen within the range of 10 to 60 minutes.
- the subsequent period is often chosen in the range of from 15 minutes to 10 hours and for many of the substrates in the range of from 15 minutes to 120 minutes.
- Some reaction can occur whilst the perborate is being introduced so that the total reaction period is often selected in the range of from 30 minutes to 10 hours, and for many substrates from 30 to to 150 minutes.
- the presence of an electron-withdrawing substituent tends to enable a shorter reaction period to be selected and an electron-donating substituent tends to demand a longer reaction period.
- the reaction can be monitored, for example by thin layer chromatography and recovery of the product commenced when the monitoring indicates that either a desired proportion of the substrate has been converted to the product, or the reaction rate has slowed thereby indicating that little further product could be obtained.
- reaction periods can be gauged in small scale trials and refined in bulk-scale operation.
- the invention process is particularly suitable for a batch style reaction procedure, but it will be recognised that by a suitable choice of reactor design such a tubular once through reactor, it is a practical proposition to carry out the reaction continuously, especially for those substrates that employ a relatively short reaction period.
- the product can be recovered from the reaction mixture by-removal of at least part of the reaction medium and preferably all of it, such as by evaporation, preferably under reduced pressure, and subsequent addition of water to the residue, thereby causing formation of a solid product.
- a suitable amount of water is often chosen in the range of 10 to 100 parts w/w per part of substrate.
- the solid can then be separated using conventional solid/liquid separating techniques such as centrifugation, filtration or settling.
- the aqueous residue comprises a saturated solution of the product. Accordingly, a further amount of product can be recovered by subsequently contacting the aqueous residue with a low molecular weight aliphatic ester such as ethyl acetate or a similar solvent having low boiling point and low miscibility with water, separating the two phases and removing the solvent, such as by evaporation, preferably under reduced pressure.
- a convenient ratio of stripping solvent to aqueous residue is often chosen in a total v/v ratio of 1:1 to 3:1.
- the conventional techniques of solvent stripping, viz continuous co- or counter-current contact or multiple batch contact are applicable.
- product losses can be reduced additionally to the solvent stripping technique or alternatively instead of that technique by recycling the aqueous residue, either before or after its contact with the above-mentioned solvent, in place of at least a fraction of the water that is added to the reaction mixture residue in an early phase of the product recovery.
- the acetic acid was removed from the reaction mixture by evaporation under reduced pressure and water, 50 mis, added to the residue.
- the solid which separated out, crude product was recovered by filtration, and dried in air.
- the - filtrate was contacted with ethyl acetate, 3 x 25 mis portions, and the combined organic phase was dried with anhydrous magnesium sulphate, and evaporated under reduced pressure, thereby precipitating a further amount of crude product.
- the two crude products were combined, dried and recrystallised to provide the yield given in the Table, which is the molar percentage of purified carboxylic acid product, based on the substrate present initially. The identity of the product was subsequently confirmed by melting point comparison with the reading given in the literature and by infra red spectral analysis.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Procédé permettant l'oxydation d'aldéhydes aromatiques par un aldéhyde ayant la formule générale (1) où n est un nombre entier entre 1 et 3, et X ou chaque X est hydrogène ou un substituant preneur d'électrons ou un substituant légèrement donneur d'électrons qui est ortho, méta ou para pour le substituant d'aldéhyde, ou un substituant fortement donneur d'électrons qui est méta pour le substituant d'aldéhyde, à condition qu'une position ortho au moins soit occupée par l'hydrogène. L'aldéhyde en question est mis en contact avec un perborate de métal alcalin et un acide acétique à une température modérée et la réaction se poursuit jusqu'à ce qu'une partie au moins de l'aldéhyde s'oxyde en un acide carboxylique aromatique correspondant.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8904798.9 | 1989-03-02 | ||
GB898904798A GB8904798D0 (en) | 1989-03-02 | 1989-03-02 | Aldehyde oxidation |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1990009975A1 true WO1990009975A1 (fr) | 1990-09-07 |
Family
ID=10652607
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB1990/000313 WO1990009975A1 (fr) | 1989-03-02 | 1990-02-28 | Oxydation d'aldehydes |
Country Status (2)
Country | Link |
---|---|
GB (1) | GB8904798D0 (fr) |
WO (1) | WO1990009975A1 (fr) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5866723A (en) * | 1991-09-25 | 1999-02-02 | Monsanto Company | Benzoyl derivatives and synthesis thereof |
US5869688A (en) * | 1994-07-20 | 1999-02-09 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US5883263A (en) * | 1996-06-20 | 1999-03-16 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1793671A1 (de) * | 1965-04-21 | 1972-03-30 | Rhone Poulenc Sa | Verfahren zur Herstellung von phenolischen Verbindungen |
DE2252674A1 (de) * | 1972-10-27 | 1974-05-09 | Bayer Ag | Verfahren zur herstellung von aldehyden aus olefinen |
-
1989
- 1989-03-02 GB GB898904798A patent/GB8904798D0/en active Pending
-
1990
- 1990-02-28 WO PCT/GB1990/000313 patent/WO1990009975A1/fr unknown
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1793671A1 (de) * | 1965-04-21 | 1972-03-30 | Rhone Poulenc Sa | Verfahren zur Herstellung von phenolischen Verbindungen |
DE2252674A1 (de) * | 1972-10-27 | 1974-05-09 | Bayer Ag | Verfahren zur herstellung von aldehyden aus olefinen |
Non-Patent Citations (1)
Title |
---|
The Merck Index, 10th Edition, 1983, Merck & Co., Inc., (Rahway, US), see page 1239, Item No. 8492,: "Sodium Perborate" * |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5866723A (en) * | 1991-09-25 | 1999-02-02 | Monsanto Company | Benzoyl derivatives and synthesis thereof |
US5869688A (en) * | 1994-07-20 | 1999-02-09 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US5973164A (en) * | 1994-07-20 | 1999-10-26 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US5986104A (en) * | 1994-07-20 | 1999-11-16 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US6121458A (en) * | 1994-07-20 | 2000-09-19 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US5883263A (en) * | 1996-06-20 | 1999-03-16 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US5900489A (en) * | 1996-06-20 | 1999-05-04 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US5910596A (en) * | 1996-06-20 | 1999-06-08 | Monsanto Company | Esterification of benzoic acid substituents of 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
US5969153A (en) * | 1996-06-20 | 1999-10-19 | Monsanto Company | Preparation of substituted 3-aryl-5-haloalkyl-pyrazoles having herbicidal activity |
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