Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C49/00—Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
  • C07C49/20—Unsaturated compounds containing keto groups bound to acyclic carbon atoms
  • C07C49/255—Unsaturated compounds containing keto groups bound to acyclic carbon atoms containing ether groups, groups, groups, or groups
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
  • C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
  • C07C45/62—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by hydrogenation of carbon-to-carbon double or triple bonds
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
  • C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
  • C07C45/67—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
  • C07C45/68—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
  • C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
  • C07C45/67—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
  • C07C45/68—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
  • C07C45/70—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms by reaction with functional groups containing oxygen only in singly bound form
  • C07C45/71—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms by reaction with functional groups containing oxygen only in singly bound form being hydroxy groups

Definitions

• This invention relates to pharmaceutically active compounds, a process for preparing and use thereof. More specifically, this invention relates to the synthesis and use of nabumetone.
• MVK methyl vinyl ketone
• US 4,061,779 discloses hydrogenation of 4-(6'-methoxy-2'-naphthyl)but-3-en-2-one to yield nabumetone as the final product.
• expensive 6-methoxy-2-naphthaldehyde is used to prepare butanone (4) and is a costly reagent.
• Netherlands patent application 8900721 discloses an alternate reaction for the production of nabumetone in which 4-chloro-2-butanone or 4-diethylamino-2-butanone is employed instead of MVK with the heterogeneous catalyst, palladium on carbon. Under the conditions described in Netherlands '721, the 4-substituted-2-butanones yield a diaryl adduct, 4,4,-di(6'- methoxynaphth-2'-yl)but-3-en-2-one, as a major or, in some cases, predominate product. Thus, methods are sought to obtain nabumetone in high yields, safely, and cost effectively.
• the present invention relates generally to chemical reactions involving the catalyzed, preferably palladium-catalyzed, coupling of aryl and vinyl halides with vinylic compounds. This reaction is typically referred to as the Heck reaction.
• Heck catalyst is generated in situ using palladium chloride and triphenylphosphine in the presence of an organic solvent, e.g., dimethylformamide.
• the present invention employs Heck technology and relates specifically to a process for the preparation of nabumetone (1) comprising contacting substituted butanone
• X is CH 3 SO 3 , OR, NR , or halogen and each R is independently hydrogen, alkyl, aryl, acyl, alkanesulfonyl, arenesulfonyl, carbamoyl, alkoxycarbonyl, or aryloxycarbonyl; with, substituted methoxynaphthalene
• the invention comprises comprising contacting
• X CH 3 SO 3 or OR and each R is independently hydrogen, alkyl, aryl, acyl, alkanesulfonyl, arenesulfonyl, carbamoyl, alkoxycarbonyl, or aryloxycarbonyl; with, substituted methoxynaphthalene
• Suitable reaction conditions generally involve temperatures in the range of about 100- 200 °C, pressures in the range of about 0-1500 psi, and reaction times in the range of about 10 min to 24 hrs.
• a catalyst preferably a homogeneous palladium catalyst is preferably generated in situ by the coupling of palladium dichloride and triphenylphosphine. The homogeneous or heterogeneous catalyst is present in an amount of about 0.005-1.0 mole % relative to the naphthalene feed.
• the reaction product of the coupling of butanone and the naphthalene derivative is then hydrogenated (with or without previous isolation) to form the desired product, nabumetone.
• This invention is concerned with a new process for the preparation of nabumetone without employing costly MVK directly. It has now been found that homogeneous palladium- catalyzed reaction of 2-bromo-6-methoxynaphthalene and 4-substituted 2-butanones produces butenone (4) in high yield,
• a preferred embodiment of the present invention involves a process for the preparation of nabumetone precursor (4) and subsequent processing to obtain the nabumetone product comprising contacting substituted butanone
• X CH 3 S0 3 , OR, NR 2 , or halogen and each R is independently hydrogen, alkyl, aryl, acyl, alkanesulfonyl, arenesulfonyl, carbamoyl, alkoxycarbonyl, or aryloxycarbonyl; with, substituted methoxynaphthalene
• the invention comprises the preparation of 4-(6'-methoxy-2'-naphthyl)-but- 3-en-2-one comprising contacting substituted butanone
• X CH 3 SO 3 , OR and each R is independently hydrogen, alkyl, aryl, acyl, alkanesulfonyl, arenesulfonyl, carbamoyl, alkoxycarbonyl, or aryloxycarbonyl; with, substituted methoxynaphthalene
• Another embodiment of the present invention is the coupling reaction of 4-substituted phenols of Formula 5
• a further alternative process for the preparation of 4-arylbut-3-en-2-ones comprises contacting under suitable conditions or substituted arene, ArY, a homogeneous palladium catalyst, and a 4-substituted 2-butanone derivative,
• X CH 3 SO 3 , OR, NR 2 , or halogen and each R independently hydrogen, alkyl, aryl, acyl, alkanesulfonyl, arenesulfonyl, carbamoyl, alkoxycarbonyl, or aryloxycarbonyl; with, substituted methoxynaphthalene
• a still further alternative process for the preparation of 4-arylbut-3-en-2-ones comprises contacting under suitable conditions a substituted arene, ArY, a heterogeneous catalyst, preferably a heterogeneous palladium catalyst, and a 4-substituted 2-butanone derivative, having the following formula
• X CH 3 SO 3 or OR and each R independently hydrogen, alkyl, aryl, acyl, alkanesulfonyl, arenesulfonyl, carbamoyl, alkoxycarbonyl, or aryloxycarbonyl; with, substituted methoxynaphthalene
• Another alternative relates to a process for preparing 4-arylbut-3-en-2-ones comprising contacting under suitable conditions a solvent, a substituted arene, ArY, and a compound selected from the group consisting of methyl vinyl ketone and a 4-substituted 2-butanone derivative having the following formula
• X CH 3 SO 3 , OR, NR 2 , or halide and each R independently hydrogen, alkyl, aryl, acyl, alkanesulfonyl, arenesulfonyl, carbamoyl, alkoxycarbonyl, or aryloxycarbonyl;
• Ar is substituted or unsubstituted phenyl or naphthyl;
• Yet another process relates to the preparation of 4-aryl-2-butanone comprising contacting under suitable conditions a 4-arylbut-3-en-2-one, a palladium catalyst, and hydrogen, in the presence or absence of a base.
• the mono aryl and diaryl adduct products are separated and assayed quantitatively by HPLC.
• reaction conditions which typically yield high monoaryl : diaryl adduct ratios with MVK feed, we have found low monoaryl : diaryl adduct ratios are obtained with MVK substitutes.
• Particular preferred MVK substitutes for the present invention include 4-hydroxy-2 -butanone and 4-acetoxy-2-butanone.
• Techniques generally employed for the present invention to make these rates comparable include using less coupling catalyst than that needed with MVK feed; adding all or a portion of the 4-substituted 2-butanone derivative to the reaction mixture throughout the reaction period rather than all at the beginning; and/or adjustment of reaction temperature. Such techniques are employed as needed to achieve an acceptably high monoaryl : diaryl adduct ratio.
• Suitable reaction conditions for the coupling of butanone and naphthyl (or aryl or arene) derivatives are generally chosen based on the specific butanone and aryl derivatives, base, catalyst, and solvent one plans to employ.
• One of skill in the art can, without undue experimentation determine ideal reaction conditions by performing initial reactions and monitoring the type and amount of byproducts formed.
• reaction temperature comprises a range of about 100-200 C C, preferably about
• Suitable pressure ranges comprise a general range of about 0-1500 psi, a preferred range of about 0-100 psi, and a most preferred range of about 0-30 psi.
• Suitable reaction times range from about 0.166-24 hrs, preferably about 0.5-8 hrs, and most preferably about 1-3 hrs. It is important to keep in mind that reaction conditions can vary significantly based on the pressure and temperature employed. Provided that the MVK formed in situ is maintained within the reaction vessel, other parameters may vary within the ranges disclosed herein. Maintaining the MVK within the reaction vessel can be accomplished by conventional techniques. For example, utilizing a sealed reactor under pressure, a reflux condenser, etc.
• a palladium (II) catalyst typically a homogenous Pd catalyst, is used for the coupling reaction and form the nabumetone precursor.
• the Pd catalyst generally results from a Pd (II) salt and a phosphine ligand compound, such as triphenylphosphine and the like.
• the most preferred catalyst is dichloro bis(triphenylphosphine)palladium (II) formed by the in situ reaction of palladium dichloride and triphenylphosphine.
• catalysts may be generated in situ from other reagents such as palladium diacetate with or without a phosphine ligand, tricyclohexylphosphine, tributylphosphine, tributylphosphite, and the like.
• the catalyst is generally employed in a catalytic amount sufficient to enable the coupling reaction. The amount is chosen based on the nature of the ketone employed. Generally, the catalyst is used in an amount of about 0.005-1.0 mole % relative to the naphthalene or arene feed, preferably in an amount of about 0.01-0.5 mole %, and most preferably in an amount of about 0.015-0.3 mole % relative to the arene feed. In some cases, for example with 4-hydroxy-2-butanone, it is appropriate to add a portion of the 4-substituted 2-butanone to the reaction mixture throughout the reaction period.
• Organic solvents to employ may be chosen from the group consisting of dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidinone, acetamide, and the like.
• the coupling reaction generally employs a base, such as potassium- or sodium carbonate, bicarbonate, or acetate, or bases such as triethylamine, and the like.
• the base acts to neutralize any acid formed from the coupling reaction which may serve to poison the catalyst.
• amines such as triethylamine, although acceptable with catalyst fed as dichlorobis(triphenylphosphine)palladium, prevent in situ generation of that catalyst from palladium dichloride and triphenylphosphine.
• 4-Acetoxy-2-butanone is a preferred MVK substitute for the coupling reaction and may be charged directly or prepared in situ from 4-hydroxy-2-butanone and either acetic anhydride or acetyl chloride.
• 4-Hydroxy-2-butanone and 3-oxobutyl mesylate, i.e., 4-mesyloxy-2-butanone are other 4-substituted 2-butanone derivative which have been employed successfully.
• Other butanone derivatives which may be employed include 4- diethylamino-, 4-(N,N-dimethylcarbamyloxy)- 4-methoxy-, and 4-benzoyloxy-2-butanone.
• 2-Methoxynaphthalene substituted at the 6 position with a halogen preferably Br and I, most preferably Br, is the preferred aryl derivative for the coupling reaction.
• suitable substituents include diazonium chloride, bromide, bisulfate, tetrafluoroborate and the like.
• Other aryl derivatives may be employed.
• the corresponding 4-hydroxyphenyl derivatives may be coupled to 4-(4'-hydroxyphenyl)but-3-en-2-one. which provides raspberry ketone on hydrogenation.
• the nabumetone precursor, or 4-arylbut-3-en-2-one coupling reaction product may be isolated by conventional means such as filtration.
• the precursor may be precipitated from the reaction mixture by addition of water, filtered, washed with water and dried. Quantitative recovery has been obtained for the precursor from such isolation.
• the precursor is carried forward to hydrogenation with a palladium on carbon catalyst without isolation of the 4- arylbut-3-en-2-one intermediate.
• An advantage of the present invention is that no such isolation is necessary.
• the coupling reaction mixture with or without filtration of potassium salts is simply carried forward to hydrogenation by addition of the palladium on carbon catalyst and application of hydrogen pressure. Removal of coupling reaction solvent and handling of said intermediate is thus avoided.
• Reaction conditions for the hydrogenation are interdependent. Suitable hydrogenation conditions include a temperature range of about 20-100 C C, a pressure range of about 15-200 psi, and a reaction time of about 0.5-24 hrs. Generally a reaction temperature of about 50 °C, pressure of about 65 psi, and reaction time of about three hours is sufficient to complete the conversion of the product of Formula 4 to nabumetone. Pressure is not a critical feature of the hydrogenation reaction, however, it does accelerate the reaction. During the hydrogenation reaction, nabumetone alcohol by-product, 7
• a basic compound such as potassium carbonate, potassium bicarbonate, potassium hydroxide, and the like, or an organic base such as an amine
• Amounts of potassium in the basic potassium compound preferably range from about 1 to about 200, more preferably about 1 to about 100. and most preferably about 1 to about 50 moles per mole of palladium in the hydrogenation catalyst. Recrystallization from isopropanol is an effective means for removing nabumetone alcohol from nabumetone.
• Methyl vinyl ketone was purchased from Janssen Chimica. 2-Bromo-6- methoxynaphthalene (BMON) was obtained from Albemarle PPC. Palladium dichloride and 5% palladium on carbon pre-wet to 50 wt % water (Engelhard's ESCAT 111) were obtained from Engelhard Corporation. N,N-Dimethylformamide (DMF) was purchased from Air Products. Triphenylphosphine was obtained from Elf Atochem North America. Potassium carbonate was purchased from Armand Products Co. and ground so that 95% passes through a 325 mesh (44 micron) sieve. Hydrogen was purchased from Big Three Industries. Celite 545 was purchased from the Celite Corporation.
• Isopropanol was purchased from Shell Corporation. 4-Hydroxy-2- butanone was purchased from TCI-EP. Acetic anhydride, methanesulfonyl chloride, 4-acetoxy- 2-butanone, acetyl chloride, methylene chloride, and triethylamine were purchased from Aldrich Chemical Company.
• Methyl vinyl ketone (27.33 g of 87.3% purity) was then added to the flask by syringe through a slightly separated side arm connection while the flask was kept under a slightly positive pressure of nitrogen.
• the contents of the reaction flask were then stirred and heated to about 132 °C, and the reaction temperature was held constant for about two hours before the contents of the flask were cooled to about 23 °C and suction filtered through 8 micron porosity filter paper.
• the reaction flask and the filtered potassium salts were washed with two portions of DMF (50.27 g total) and the DMF washes were suction filtered into the coupling reaction mixture filtrate. Approximately 99% of the starting BMON had been converted.
• Monoaryl adduct diaryl adduct were observed in a 95.5 : 4.5 ratio, as determined by HPLC peak area ratio.
• the contents of the reaction flask were then stirred and heated to about 132 °C, and the reaction temperature maintained for about two hours before the contents of the flask were cooled to about 48.5 °C and suction filtered through 8 micron porosity filter paper.
• the reaction flask and the filtered potassium salts were washed with two portions of DMF (95.03 g total), and the DMF washes were suction filtered into the coupling reaction mixture filtrate. Approximately 98.9% of the starting BMON had been converted. Mono aryl adduct and diaryl adduct were observed in a 95.5 : 4.5 HPLC peak area ratio, and were the only major products observed.
• the autoclave was vented and purged with nitrogen as previously described.
• the conversion of monoaryl adduct was greater than about 99.7%, and nabumetone and nabumetone alcohol were present in about a 98.96 : 1.04 F.I.D. G.C. peak area ratio.
• Celite (2.1025 g) was mixed into the hydrogenation reaction mixture, which was then suction filtered through 8 micron porosity filter paper.
• the autoclave and the filtered solids were washed with two portions of DMF (18.11 g total), and the DMF washes were suction filtered into the hydrogenation reaction mixture filtrate.
• DMF was then removed from the combined DMF hydrogenation reaction mixture and wash liquor filtrates by simple vacuum distillation at about 30.5 torr and undistilled residue temperatures rising to about 92.3 °C. While still molten (80-100 °C), the undistilled residue was then suction filtered through 8 micron filter paper to remove potassium salts which had precipitated during the removal of the DMF by vacuum distillation.
• the filtrate was crude nabumetone. Distillation of Crude Nabumetone. The crude nabumetone was vacuum distilled. The distilled nabumetone weighed about 53.17 g (84.7% yield). The undistilled residue weighed about 8.72 g and contained a significant amount of nabumetone.
• Example 1 was repeated with the following modifications to the coupling reaction.
• the coupling reaction mixture charge consisted of BMON (81.19 g), DMF (620 mL), potassium carbonate (42.42 g), palladium dichloride (0.0064 g). triphenylphosphine (0.018 g), and, instead of MVK, 4-hydroxy-2-butanone (24.11 g).
• BMON 81.19 g
• DMF 620 mL
• potassium carbonate 42.42 g
• palladium dichloride 0.0064 g
• triphenylphosphine 0.018 g
• 4-hydroxy-2-butanone 24.11 g
• 4-hydroxy-2-butanone 18.43 g was added by addition funnel from a fourth reaction flask neck over about two hours.
• Example 4 Use of 4-Hydroxy-2-butanone Instead of MVK Example 3 was repeated utilizing palladium dichloride (0.009 g), triphenylphosphine
• Crude 4-acetoxy-2-butanone was prepared as follows. A mixture of 4-hydroxy-2- butanone (101.48 g) and acetic anhydride (131.05 g) was stirred and heated to about 120 °C for about 40 minutes before the acetic acid by-product was removed by vacuum distillation at about 24 torr and vapor temperatures rising to about 49 °C. The distillation residue was about 129.0 g of crude 4-acetoxy-2-butanone.
• Example 1 was repeated on half scale with the following additional modifications to the coupling reaction.
• BMON 32.64 g
• DMF 250 mL
• potassium carbonate 30.92 g
• palladium dichloride 3.55 mg
• triphenylphosphine 9.23 mg
• MVK 22.86 g
• Example 1 was repeated at half scale with the following additional modifications to the coupling reaction.
• a 500 mL flask was charged with just DMF (250 mL) and potassium carbonate (31.26 g) before being purged with nitrogen.
• 4-Hydroxy-2-butanone (15.80 g) instead of MVK was then added by syringe, and the resulting mixture was stirred and cooled to about 0
• Example 1 was repeated at quarter scale with the following additional modifications to the coupling reaction.
• a 250 mL reaction flask was charged with BMON (16.28 g), DMF (124 mL), potassium carbonate (9.49 g), palladium dichloride (0.12 g), triphenylphosphine (0.3508 g), and, instead of MVK, freshly prepared crude 4-mesyloxy-2-butanone (15.50 g).
• the reaction mixture had been stirred magnetically at about 132 °C for about two hours, about 24.5% of the starting BMON had been converted.
• Monoaryl adduct was the only major product observed.
• Example 6 was repeated with the additional modification that water (550 mL) was added to the combined coupling reaction mixture and wash filtrates to precipitate a yellow solid. After filtration, washing with water (400 mL), and vacuum drying at about 14 torr and about 56 °C for about 72 hours, the solid, crude monoaryl adduct isolated, weighed about 30.96 g (99% crude yield).

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• 1996
  • 1996-05-10 EP EP02004992A patent/EP1223156A1/de not_active Withdrawn
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