CATALYSED FLUORINATION OF CARBONYL COMPOUNDS

Abstract: The present invention provides a method of substituting a carbonyl compound with fluorine at the alpha -position, comprising reacting the carbonyl compound with a fluorinating agent in the present of a metal-containing catalyst. The reaction results in replacement of a hydrogen atom by fluorine. The catalyst, which is used in a catalytically effective amount, is preferably a transition metal. In one class of methods the catalyst is a transition metal compound. In another class of methods, the catalyst is an elemental metal, in which case the carbonyl compound has an activating group attached to the carbon atom which is substituted by fluorine.

Description: CATALYSED FLUORINATION OF CARBONYL COMPOUNDS This invention relates to the fiuorination of organic compounds, in particular, to the fluorination of carbonyl compounds especially those having a carbonyl, nitro, nitrile sulphonyl or phosphoryl group in the 3 -position to the carbonyl group, notably 1,3- dicarbonyl compounds (also known as β-dicarbonyl compounds). Fluorinated carbonyl compounds, for example fiuorinated 1,3-dicarbonyl compounds, are very valuable intermediates in the synthesis of other fluorine- containing compounds. International Patent Application No PCT/GB94/02547 describes how treating solutions of 1,3-dicarbonyl compounds in various solvents with elemental fluorine gives the corresponding 2-fluoro-1.3-dicarbonyl compounds. Unfortunately, the fluorination of certain 1,3-dicarbonyl compounds proceeds at an undesirably low rate. Surprisingly, we have now found that the fluorination not only of 1,3-dicarbonyl compounds but also of other carbonyl compounds is catalysed by compounds of transition metals. The present invention provides a method of substituting a carbonyl compound with fluorine at the α-position, comprising reacting the carbonyl compound with a fluorinating agent in the presence of a metal-containing catalyst. The reaction results in replacement of a hydrogen atom by fluorine. The catalyst, which is used in a catalytically effective amount, is preferably a transition metal. In one class of methods the catalyst is a transition metal compound. In another class of methods, the catalyst is an elemental metal, in which case the carbonyl compound has an activating group attached to the carbon atom which is substituted by fluorine. The invention also provides a method of fluorinating a 1 ,3-dicarbonyl compound comprising reacting the 1,3-dicarbonyl compound with a fluorinating agent in the presence of a compound of a transition metal. The reaction results in replacement of a hydrogen atom by fluorine. A further aspect resides in a process for the fluorination of a β-dicarbonyl compound by means of a fluorinating agent, the process being carried out in the presence of a metal-containing catalyst, the metal preferably being a transition metal. Methods Catalysed by a Transition Metal Compound The transition metal compound is preferably a salt. The transition metal is usually a first row transition metal. Exemplary transition metals are those of Groups Vila, VIII, lb and lib. More specific examples of compounds which may be used as catalysts in a method of the present invention are salts and other compounds of copper, iron, cobalt, nickel, manganese or zinc. The identity of the anion of the salt is not critical; suitably it is nitrate, sulphate or acetate, of which nitrate is particularly convenient. A mixture of compounds of two or more metals may be used. Any amount of catalyst may be added to the fluorination reaction but the amount is suitably up to 25 gram atoms of transition metal ion, and preferably 0.2 to 2.5 gram atoms, to 100 moles of substrate. More preferably, the amount of catalyst added is in the range 0.5 to 10 gram atoms of transition metal ion to 100 moles of substrate. A preferred fluorinating agent is elemental fluorine. The carbonyl group serves to activate the α-hydrogen which is replaced. The method works well with, inter alia, compounds in which the carbonyl group is ketonic but this feature is far from critical (for example, esteric carbonyl groups are also very suitable). The compounds which are fluorinated preferably have another activating group attached to the carbon atom which is substituted by fluorine, for example another CO group or (R θ)2PO, SO2 or CN; R.I is in principle any organic group compatible with the reaction, e.g. alkyl, cycloalkyl or aryl. 1,3-Dicarbonyl compounds are a very preferred class of carbonyl compounds. More particularly, the starting compounds are preferably of the formula (A): RCO.CHR^R 2 , where: R is selected from the group consisting of alkyl, oxyalkyl (i.e. -O-alkyl), cycloalkyl, oxycycloalkyl, aryl and oxyaryl; R 1 is selected from the group consisting of CO.R 3 , CO.OR 3 , NO2, CN, CO.NR 3 2 , SO 2 R 3 and PO.(OR 3 )2, wherein R 3 is alkyl or cycloalkyl, and R 2 is selected from the group consisting of H. F, Cl, NO 2 , CN, alkyl, oxyalkyl, cycloalkyl, oxycycloalkyl, aryl and oxyaryl; or wherein R and R 1 are joined together to form a cycloalkyl structure, or R 1 and R 2 are joined together to form a cycloalkyl or aryl structure, or R and R 1 as well as R 1 and R 2 are so joined, the two ring structures being fused, any of the aforesaid alkyl, cycloalkyl and aryl moieties optionally being substituted. More preferably, the fluorination reaction is the fluorination of compounds having the general formula (B): RCO.CHR'CO.R" into compounds having the general formula RCO.CFR'CO.R". In these formulae, the group R may be alkyl, substituted alkyl, cycloalkyl, aryl, or substituted aryl, R' may be hydrogen, chlorine, nitro, cyano, alkyl, substituted alkyl, cycloalkyl, aryl, or substituted aryl, and R" may be alkyl, substituted alkyl, cycloalkyl, aryl, substituted aryl, OR, NR 2 . Further, the groups R and R' may be joined together to form a cyclic structure. Where in the starting material for the fluorination reaction R' is H, the product of the reaction may have the formula RCO.CF 2 CO.R". For the compounds of formulae A and B suitable substituents include R and R 2 groups or, as the case may be, R and R' groups; for example, alkyl may be substituted chlorine or fluorine), alkoxy and aryloxy. as well as other groups which are relatively inert to fluorine. Any of the aforegoing substituents may be substituted in turn by one or more other suitable substituents, to form groups such as. for example, haloalkoxy or alkoxyaryl. The number of atoms in any of the groups R, R 1 and R 2 of formula (A), R, R and R" of formula (B) and R ! is not critical, since they play no part in the reaction. By way of example, however, the organic moieties may contain up to 10 carbon atoms, e.g. 1 to 4 carbon atoms. Cyclohexyl and cyclopentyl may be mentioned as a suitable cycloalkyl groups, and phenyl and naphthyl as suitable aryl groups, amongst others. Methods Catalysed by Elemental Metal In methods of this class, the catalyst is in the form of an elemental metal. A particular example of such a catalyst is metallic copper which may be used in the form of, for instance, a powder. The carbonyl compound has an activating group in the β -position to the carbonyl group, like the preferred carbonyl reactants used with the transition metal compound catalysts. Indeed, the preferred compounds described with reference to the transition metal compounds are preferred also for the metal catalysts. Most preferably, the compound is a β-dicarbonyl compound. Preferably, the β-dicarbonyl compound is a haloacetoacetate. more preferably a chloroacetoacetate. Preferably, the catalyst is used in a small amount. Particularly in the case of metallic copper, a preferred amount is up to 50 mg (8 x 10 grams atom) per 100ml of reactant solution, more preferably 10 to 30 mg (1.6 x 10 to 4.7 x 10 grams atom) 100ml solution and most preferably about 20 mg (3.15 grams atom) per 100ml. Typically, the metal is used in an amount of up to 0.04 gram atoms, and desirably up to 0.02 gram atoms, per mole of β-dicarbonyl compound, more preferably 0.004 to 0.012, especially about 0.008 gram atoms per mole of compound. It is possible that the catalyst operates to speed up the enolisation of the compound carbonyl. Reaction Conditions Preferably, the reactions of the invention are conducted in the presence of a solvent. Preferred solvents include formic acid, acetic acid and acetonitrile, the latter being preferably used with a little water to give solubility to the salts. Where fluorine is used as the fluorinating agent, it is preferably diluted with an inert gas such as nitrogen. Preferably, the fluorine is diluted to 1-50% v/v and. preferably in the range 5-20% v/v. The temperature of the reaction is preferably 0-10 °C. The substrate may be used in a wide concentration range, preferably up to 400 grams/ litre of solvent. Examples of the present invention will now be described, by way of illustration only. EXAMPLES Example 1 By way of a control example, a reaction without any added salts was carried out. Thus, a glass reaction vessel fitted with a PTFE coated mechanical stirrer, a FEP (fluorinated ethylene-propylene) thermocouple well and FEP gas delivery tube was charged with ethyl-2-chloroacetoacetate (3.29 gm., 20 mmol.) and formic acid (50 ml) before being cooled to 5-8 °C. The vessel was purged with nitrogen and then fluorine (32mmol) diluted to 10% v/v with nitrogen was passed through the stirred solution over a period of two hours. At the end of this treatment, the fluorine supply was turned off and the reaction vessel was purged with nitrogen. The reaction mixture was then poured into water and extracted with dichloromethane. The extracts were dried, evaporated and the colourless residue was analysed by glc which showed that 16% of the ethyl chloroacetoacetate had been converted into ethyl-2- chloro-2-fluoroacetoacetate. A series of experiments was carried out to illustrate the effect of adding certain salts, in varying amounts, to the a reaction carried out as described above. The results of these experiments are shown in the following Table. Experiment No. Salt added Amt Salt g atom cation lOO Conversion, % added, mmol g mol substrate Control - - - 16 Ex. 1 Fe(NO 3 ) 3 9H 2 0 0.4 2 54 Ex. 2 Fe(NO 3 ) 3 9H 2 O 4.0 20 75 Ex. 3 Co(NO 3 ) 2 6H 2 O 0.4 2 85 Ex. 4 NiSO 4 6H 2 O 0.4 2 50 Ex. 5 Cu(N0 3 ) 2 3H 2 0 0.4 2 90 Ex 6 Cu(OAc) 2 H 2 0 0.4 2 84 Ex 7 Ni(NO 3 ) 2 6H 2 0 4.0 20 53 Ex 8 Zn(NO 3 ) 2 6H 2 O 0.4 2 62 Ex 9 Mn(NO 3 ) 2 6H 2 O 0.4 2 60 Example 2 A glass reaction vessel fitted with a PTFE coated mechanical stirrer, an FEP thermocouple well and FEP gas delivery tube was charged with diethyl malonate (3.2 gm., 20 mmol.), cupric nitrate 3H 2 O (0.48gm., 2.0 mmol.) and acetonitrile (50 ml.) before being cooled to 5-8 °C. The vessel was purged with nitrogen and then fluorine diluted to 10% v/v with nitrogen was passed through the stirred solution at a rate of 16 mmol / hour for 4 hours. At the end of the treatment, the fluorine supply was turned off and the reaction vessel was purged with nitrogen. The reaction mixture was then poured into water and extracted with dichloromethane. A weighed amount of trifluoromethylbenzene was added to the extracts whose 19 F nmr spectrum was then measured. The dried extracts were evaporated and the residue was analysed by glc and or l H nmr. From this information, the amount of substrate converted (conversion) and yield of product, based on the amount of substrate converted, were calculated. A sample of pure product was obtained by preparative scale gc and its identity was confirmed as diethyl-2-fTuoromalonate {5H 1.41 (6H, t, JHH 7.13, C_ 3 ), 4.42 (4H, q, J H H 7.2, CH 2 ), 5.36 (1H, d, J H F 48.3, CHF); δ F 196.5 (d, J H F 48.2); δ c 13.9 (s, CH 3 ), 62.7 (s, C__ 2 ), 85.3 (d, ! j C F 196.6, CHF), 163.9 (d. 2 J C F 24.1, CO); m/z (CI + , NH 3 ) 196 ((M+NH 4 ) + , 100%)}; Conversion 100%, Yield 78%. Example 3 In an experiment carried out as described in Example 2 but in the absence of any transition metal compound, the conversion was less than 5%. Example 4 An experiment was carried out as described in Example 2 using diethyl nitromalonate instead of diethyl malonate. Thus, 4.1 gm. (20mmol.) diethylnitromalonate was treated with fluorine to give diethylfluoronitromalonate (δ H 1.40 (6H, t, J HH 7.11, CH 3 ), 4.47 (4H, q, J HH 7.12, CH 2 ); δ F 127.3 (s); δ c 13.7 (s, CΗ 3 ), 65.2 (s, CH 2 ), 106.3 (d, 1J C F 261.7, CF), 157.9 (d. J C F 25.2, CO).} in 76% yield. The conversion was 97%. Example 5 When the experiment in Example 4 was repeated in the absence of cupric nitrate 3H 2 O, the conversion was ca. 12%. Example 6 Example 2 was repeated using less copper nitrate and a shorter exposure to fluorine. Thus, 3.2 gm. (20mmol.) diethylmalonate and 0.096gm. (0.4mmol.) copper (II) nitrate 3H 2 0 in 50 ml acetonitrile were treated with 32 mmol. fluorine, diluted to 10% v/v with nitrogen, over 2 hours to give diethylfluoromalonate in high yield. Conversion. 88%. Example 7 Example 6 was repeated using O.l lόgm. (0.4mmol.) nickel nitrate 6H 2 0 instead of copper nitrate. Conversion 70%. Example 8 Example 6 was repeated using ethyl acetoacetate instead of diethyl malonate. 45% of the ethyl acetoacetate reacted to give ethyl-2-fluoroacetoacetate in high yield (80%). Example 9 When Example 8 was repeated in the absence of a compound of a transition metal, the conversion was 23%. Example 10 Example 6 was repeated using N,N-diethylamino acetoacetamide instead of diethyl malonate. After this treatment, 59% of the N,N-diethylamino acetoacetamide reacted to give N,N-diethylamino-2-fluoroacetoacetamide {(Found: C, 54.3; H, 8.1 ; N, 7.8. C8H14NO2 requires C, 54.8; H, 8.0; N, 8.O.); δ H 5.3 (d, J H F 49.9, 1H, -CHF-), 3.26 (m, 4H, NCH 2 CH 3 ), 2.18 (d, J = 4.0, 3H, CH 3 COCHF), 1.08 (t, J =7.2, 3H, - CH 2 CH 3 ), 1.00 (t, J =7.0, 3H, -CH 2 CH 3 ); δ F -188.7 (dd, F Η F 49.5, J Η Η 4.3); δ c 201.7 (d, 2 J C F 24.0, CΗ 3 COCΗF-), 162.8 (d, 2 J CF 20.2, CO.N<), 91.25 (d, l ] C ¥ 194.9, CHF), 41.47 (s, CH 2 CH 3 ), 40.41 (s, CH9CH3), 25.73 (s, CH 3 CO), 13.90 (s, CH2CH 3 ), 12.20 (s, CH 2 CH 3 ); m/z, 175}. Example 11 When Example 10 was repeated in the absence of a compound of a transition metal, the conversion was 46%. Example 12 Example 2 was repeated using ethyl cyanoacetate instead of diethyl malonate. After this treatment, 46% of the starting material was converted and the yield of ethyl cyanofluoroacetate {(HRMS (NH3/CI*), Found: 149.0730; C 5 Hι 0 FN 2 O 2 (M+NH 4 )+ requires 149.0726); δ H 1.39 (t, J H ,H 7.14, CH 3 ), 4.42 (q, J H ,H 7.14, CH 2 ), 5.50 (d, J H ,F 46.3, CHF); δ F -194.6 (d, J Η ,F 46.3); δ c 13.89 (s, CΗ 3 ), 64.31 (s, (CH 2 ), 74.28 (d, l J c, F 196.8 CFH), 111.62 (d, J C ,F 29.8, CN), 160.64 (d, J C ,F 24.7, CO).} was 50% and the yield of the ethyl cyanodifluoroacetate was 8%. *CI = Chemical Ionisation Example 13 When Example 12 was repeated in the absence of a compound of a transition metal, the conversion was ca. 12%. Example 14 Example 2 was repeated using ethyl nitroacetate instead of diethyl malonate. After this treatment, 54% of the starting material was converted and the yield of ethyl nitrofluoroacetate { (HRMS (CH 4 /CI), Found: 152.0312; C 4 H 7 FNO 4 (M+l)+ requires 152.0391); δ H 1.38 (t, J H ,H 7.1. CH 3 ), 4.42 (q, J Η ,Η 7.1, CH 2 ), 6.06 (d, J Η ,F 46.4, CHF); δ F -150.5 (d, J Η ,F 48.4); δ c 13.75 (s, CΗ 3 ), 64.58 (s, (CH 2 ), 102.72 (d, Ϊ JCF 248.9 CFH), 159.0 (d, 2 J C ,F 24.8, CO).} was 52% and the yield of ethyl difluonitroacetate {δ F -92.8 (s); δ H 1.41 (t, J H ,H 7.1, CH 3 ), 4.49 (q, J Η ,Η 7.1, CH 2 ); δ c 13.6 (s. CΗ 3 ), 65.8 (s, (CH 2 ), 112.9 (t, lJ c>F 297.5 CF 2 ), 155.9 (t, 2 J C , F 31.3, CO).} was 21%. Example 15 When Example 14 was repeated in the absence of a salt of a transition metal, the conversion was ca. 12%. Example 16 Example 2 was repeated using 4,4-dimethyl-3-oxo-2-pentane nitrile instead of diethyl malonate. After this treatment, 70% of the starting material had reacted and the yield of 4,4-dimethyl-3-oxo-2-fluoropentane nitrile { (HRMS (NH3/CI), Found: 161.1090; C 7 Hι 4 FN 2 O (M+NH4) + requires 161.1090); δ H 1.31 (9H, s), 5.69 (1H, d, J H ,F 47.0); δ F -192 (d, J H ,F 47.0); δ c 25.76 (d, 4 j C F 2.3, CH 3 ), 44.29 (d, 3 J C,F 2.7, (CH 3 ) 3 C ), 79.08 (d, lJ c>F 199.2. CFH), 112.29 (d, 2 J C ,F 29.7, CN), 200.59 (d, 2j C,F 17.9, CO).} was 52%. The yield of 4,4-dimethyl-3-oxo-2,2-difluoropentane nitrile {δ F -94.2 (s); δ H 1.34 (s); δ c 30.02 (s, CH 3 ), 47.68 (s, (CH 3 ) 3 C ), 109.63 (t, !JC,F 262.47 CF 2 ), 114.25 (t, 2 J C ,F 42.14, CN), 200.40 (t, 2 J C ,F 25.34, CO); m/z (CI + , CH 4 ) 162 (M+l).}was 13% Example 17 When Example 16 was repeated in the absence of a salt of a transition metal, the conversion was ca. 15%. Example 18 Example 2 was repeated using dimethyl-2-oxypropyl phosphonate instead of diethyl malonate. After this treatment, 95% of the starting material was converted and the yield of dimethyl- 1 -fluoro-2-oxypropyl phosphonate (purified by column chromatography; SiO 2 /ethyl acetate) {(HRMS, Found: (M+NH 4 ) + 202.0644 C 5 Hι 4 FNO 4 P requires 202.06445); δ H 2.39 (3H, d, 4 J H ,F 4.5, CO.CH 3 ), 3.9 (6Η, d, d, J H ,p 10.8, J 2.9, CH 3 OP), 5.25 (1Η, d,d, 2 J Η ,F 47.7, 2 J Η ,p 14.4, CHF); δ F -208 (d,d,q, 2 J F ,P 71.3, 2 J Η, F 47.8, 4 J Η ,F 4.5); δ P 12.7 (d, 2 J F,P 71.2); δ c (50MΗz) 26.5 (s, CH 3 O.C), 54.2 (d,d, 2 J C, p 6.6, 4 j C)F 2.0, CH 3 OP), 91.0 (d,d, » J C ,F 196.5, lJ CjP 152.5 CHF), 200.5 (d, 2 J C ,F 20.2, CFHCO); m z (CI + , NH 3 ) 202 ((M+NH 4 ) + , 10%), 128 (100).} was 20% and the yield of dimethyl- l,l-difluoro-2-oxypropyl phosphonate was ca.5%. Example 19 When Example 18 was repeated in the absence of a salt of a transition metal, the conversion was ca. 5%. Example 20 Example 2 was repeated using methanesulphonylpropan-2-one instead of diethyl malonate. After this treatment. 95% of the starting material was converted and the yield of l-fluoro-l-methanesuphonylpropan-2-one (purified by column chromatography; SiO 2 /dichloromethane) {(Found: C, 31.0; H, 4.4. C 4 H 7 FO3S requires C, 31.2; H, 4.5%, HRMS, Found; (M+N__4) + 172.0444 C4H11FNO3S requires 172.04437); δ H 2.5 (3H, d, 4 J H ,F 3.6, CO.CH 3 ), 3.1 (3Η, d, 4j H)F 2.2, SO.CH 3 ), 5.6 (1H, d, J H , F 48.0, CHF); δ F -183.7 (dm, 2 J Η)F 47.0); δ c 27.8 (s, CH 3 S), 38.1 (s, CH 3 C), 100.4 (d, 1J C ,F 231.CHF), 196.0 (d, J C)F 20.4, CO); m z (CI + , NH 3 ) 172 ((M+NH 4 ) + , 100%).} was 45% and the yield of 1,1-difluoro-l- methanesuphonylpropan-2-one { δ F -1 13.3 (s); m z (CI + . NH 3 ) 190 ((M+NH 4 ) + , 100%).} was ca. 5%. Example 21 When Example 20 was repeated in the absence of a salt of a transition metal, the conversion was ca. 14%. Example 22 To a solution of 5.0g ethyl chloroacetoacetate in 100ml formic acid was added 20mg of copper powder. This was stirred at 3 ° C while a gaseous mixture of nitrogen (60ml/min) and fluorine (6.7ml/min) was passed through for 6 hours. The reaction mixture was periodically analysed by GC by taking out an aliquot, drowning into water and extracting with dichloromethane. The results are shown in Table 1 and in Figure 1 of the accompanying drawings. Table 1 GC results - integration Time in hours %conversion 1 20.0 1.5 25.7 2 35.7 2.5 42.9 3 55.6 3.5 60.4 5 78.8 6 87.3 Example 23 The same procedure was used as in Example 22, except that 20mg of copper powder were added to the reaction solution after it had proceeded for 4.5 hours. The results in this case are given in Table 2 and in Figure 2 of the accompanying drawings. Table 2 GC results - integration Time in hours %conversion 0.5 7.1 1 12.2 1.5 16.5 2 19.9 2.5 24.9 3.5 28.6 4 33.2 4.5 37.3 20mg of copper powder added 5 44.0 6 58.2 6.4 65.7 Example 24 The same procedure was used as in Example 22, except that lg of copper powder was added at the beginning of the reaction and a further lg after 5.25 hours. The results are given in Table 3 and in Figure 3 of the accompanying drawings. Table 3 GC results integration Time in hours %conversion copper added 0.5 6.2 1 12.0 1.5 12.5 2 14.4 2.5 15.3 3.5 16.7 5.25 22.3 1 g of copper powder added 5.5 27.5 5.6 28.4 6.5 32.6 Example 25 The same procedure was used as in Example 22, except that lg of copper powder was added to the reaction after 6 hours. The results are given in Table 4, and in Figure 4 of the accompanying drawings. Table 4 GC results - integration Time in hours %conversion 0.3 6.6 0.8 8.9 1.5 18.0 2.2 18.4 3 21.1 3.5 24.5 5 31.7 5.7 34.2 1 g copper powder added 6.3 43.1 6.7 47.2 Example 26 The same procedure was used as in Example 22, except that 30mg of potassium fluoride were added at the beginning of the reaction and 20mg of copper powder were added after 5.5 hours. The results are given in Table 5 and in Figure 5 of the accompanying drawings. Table 5 GC results - integration Time in hours %conversion 0.5 2.7 1 4.4 1.77 7.7 2 8.9 3 12.0 3.5 13.9 4.8 21.6 5.5 26.4 20mg of copper powder added 6 29.1 6.5 35.0 7 43.9 7.4 50.2 The above examples 22-26 show that when very small amounts of metallic copper are added, the reaction is speeded up. This occurs both when the copper is added from the start (Example 22) and when the copper is added part-way through the reaction (Example 23). If, however, a larger quantity (about lg per 100ml) is added during the reaction (Examples 24and 25), there is an initial increase in rate, following which the reaction slows down again. If a larger quantity of copper is added at the start there is no catalysis at all (Example 24). Example 26 investigates the possibility that the reaction is being catalysed by base, for instance fluoride ion from copper fluoride. Traces (30mg) of potassium fluoride were added at the beginning of the reaction. There was no reaction rate increase but rather a slowing down. Addition of 20mg of copper powder after 5.5 hours resulted in an increase in the reaction rate.

Claims: CLAIMS 1. A method of substituting a carbonyl compound with fluorine at the α-position by replacement of a hydrogen atom, comprising reacting the carbonyl compound with a fluorinating agent in the presence of a catalytically effective amount of a metal-containing catalyst, the carbon atom which is substituted by fluorine being attached to an activating group additional to said carbonyl group when the metal- containing catalyst is an elemental metal. 2. A method according to Claim 1 wherein the catalyst is a transition metal compound. 3. A method according to Claim 2 wherein the compound is a salt of copper, iron, cobalt, nickel, manganese or zinc. 4. A method according to Claim 2 or Claim 3 wherein the transition metal compound is present in the range of from 0.2 to 25 gram atoms of transition metal ion to 100 moles of carbonyl compound. 5. A method according to any of the Claims 2 to 4 wherein the transition metal compound is ferric nitrate, cobalt nitrate, nickel sulphate or copper nitrate. 6. A method according to any of Claims 2 to 5 wherein the carbon atom which is substituted by fluorine is also attached to another activating group, for example another CO group, (R'O) 2 PO, SO 2 or CN. 7. A method according to Claim 6 wherein the carbonyl compound is an α- substituted carbonyl compound having the general formula RCO.CHR^R 2 , where: R is selected from the group consisting of alkyl, oxyalkyl (-O-alkyl), cycloalkyl, oxycycloalkyl, aryl and oxyaryl; R 1 is selected from the group consisting of CO.R 3 , CO.OR 3 , NO 2 , CN, CO.NR 3 2 , SO 2 R 3 and PO.(OR 3 ) 2 , wherein R 3 is alkyl or cycloalkyl, and R 2 is selected from the group consisting of H, F, Cl, NO 2 , CN, alkyl, oxyalkyl, cycloalkyl, oxycycloalkyl, aryl and oxyaryl; or wherein R and R 1 are joined together to form a cycloalkyl structure, or R 1 and R 2 are joined together to form a cycloalkyl or aryl structure, or R and R 1 as well as R 1 and R 2 are so joined, the two ring structures being fused, any of the aforesaid alkyl, cycloalkyl and aryl moieties optionally being substituted. 8. A method according to Claim 7 wherein the carbonyl compound is of the formula RCO.CHR'COR" where R is selected from the group consisting of alkyl, substituted alkyl, cycloalkyl, aryl and substituted aryl, R is selected from the group consisting of hydrogen, chlorine, nitro, cyano, alkyl, substituted alkyl, cyclo alkyl, aryl and substituted aryl, and R" is selected from the group consisting of alkyl, substituted alkyl, cyclo alkyl, aryl, substituted aryl, OR and NR, or wherein the groups R and R are joined together to form a cyclic structure. 9. A method according to Claim 7 wherein R is selected from the group consisting of alkyl, oxyalkyl, cycloalkyl and oxycycloalkyl, any of the aforesaid moieties optionally being substituted. 10. A method according to Claim 7 or Claim 9 wherein R 2 is selected from the group consisting of H, alkyl, oxyalkyl, cycloalkyl and oxycycloalkyl, aryl and oxyaryl, any of the aforesaid moieties optionally being substituted. 11. A method according to any of Claims 7, 9 and 10 wherein R 1 is selected from the group consisting of CO.R 3 and CO. OR 3 . 12. A method according to any of Claims 7 to 11 wherein any one or more of R, R', R 2 , R 3 , R' and R" contains up to 10 carbon atoms. 13. A method according to Claim 1 wherein the carbonyl compound is a β- dicarbonyl compound and the catalyst is a transition metal catalyst. 14. A method according to Claim 13 wherein the catalyst is in the form of elemental metal. 15. A method according to Claim 14 wherein the catalyst is metallic copper in powder or another form. 16. A method according to Claim 14 or Claim 15 wherein the elemental metal is used in an amount of no more than 0.04 gram atoms, and preferably of from 0.004 to 0.02 gram atoms, per mole of β-dicarbonyl compound. 17. A method according to any of Claims 13 to 16 wherein the β-dicarbonyl compound is as defined by any of Claims 6 to 12 and optionally is a haloacetoacetate. 18. A method according to Claim 17 wherein the haloacetate is a chloroacetoacetate. 19. A method according to any of the preceding claims wherein the fluorinating agent is elemental fluorine. 20. A method according to Claim 19 wherein the fluorinating agent is fluorine gas diluted with an inert gas. 21. A method according to Claim 20 wherein the fluorine gas is diluted to 1 -50??. 22. A method according to any of the preceding claims wherein the reaction temperature is 0-10°C 23. A method according to any of the preceding claims wherein the carbonyl compound is initially present in an amount up to 400 grams/litre of solvent. 24. A method of fluorinating a 1,3-dicarbonyl compound comprising reacting the 1,3-dicarbonyl compound with a fluorinating agent in the presence of a salt of a transition metal. 25. A method according to Claim 24 which further includes the feature(s) recited in one or more of Claims 3, 5, 8 or 19 to 23. 26. A process for the fluorination of a β-dicarbonyl compound by means of a fluorinating agent, the process being carried out in the presence of a metal-containing catalyst, the metal preferably being a transition metal. 27. A process according to Claim 26 which further includes the feature(s) recited in one or more of Claims 14 to 18. 28. A process according to any of Claims 1 to 27 wherein the fluorinated carbonyl compound is subjected to one or more further processes to make a subsequent end product.

Inventors: CHAMBERS RICHARD DICKINSON, HUTCHINSON JOHN, MOILLIET JOHN STEWART, CHAMBERS, RICHARD, DICKINSON, HUTCHINSON, JOHN, MOILLIET, JOHN, STEWART
Applicants: CHAMBERS RICHARD DICKINSON, F2 CHEMICALS LIMITED, HUTCHINSON JOHN, MOILLIET JOHN STEWART, CHAMBERS, RICHARD, DICKINSON, HUTCHINSON, JOHN, MOILLIET, JOHN, STEWART
Application year: 1998
Main classification: C07B39
IPC codes: C07B39, C07C45, C07C67, C07C69, C07C201, C07C205, C07C231, C07C235, C07C253, C07C255, C07C315, C07C317, C07F9