Singlet oxygen oxidation of organic substrates

[0001] The only singlet oxygen oxidation (1O2-Ox) which is currently carried out industrially is the photochemical 1O2-Ox in which the 1O2 is generated by a photochemical route. The disadvantage of this process is the high cost of the photochemical equipment required, and also a limited service life. The lamps required degenerate relatively rapidly during the oxidation as a result of the glass surface becoming dirty. In addition, this process is not suitable for colored substrates. The process is actually suitable only for fine chemicals which are produced on a relatively small scale. (La Chimica e I'Industria, 1982, Vol. 64, page 156)

[0002] For this reason, attempts have been made to find other process variants for the 1O2-Ox which are suitable for the 1O2-Ox of non-water-soluble, hydrophobic organic substrates.

[0003] J. Am. Chem. Soc., 1968, 90, 975 describes, for example, the classical “dark” 1O2-Ox in which 1O2 is generated not photochemically, but chemically. In this process, hydrophobic substrates are oxidized by means of a hypochlorite/H2O2 system in a solvent mixture of water and organic solvent. However, this process has found only a few synthetic applications since many substrates are only sparingly soluble in the required medium. Furthermore, the potential use is somewhat limited due to secondary reactions between hypochlorite and substrate or solvent. Furthermore, a large part of the 1O2 is deactivated in the gas phase. In addition, this process is not suitable for the industrial scale since attachment of the hypochlorite onto H2O2 is brought about in the organic medium, and a large excess of H2O2 is required to suppress the secondary reaction of substrate with hypochlorite. An additional disadvantage arises as a result of the formation of stoichiometric amounts of salt.

[0004] One variant of the “dark” 1O2-Ox which is not based on hypochlorite and thus should partly avoid the above disadvantages is known, for example, from J. Org. Chem., 1989, 54, 726 or J. Mol. Cat., 1997, 117, 439, according to which some water-soluble organic substrates are oxidized with H2O2 and a molybdate catalyst in water as solvent. According to Membrane Lipid Oxid. Vol. 11, 1991, 65, the 1O2-Ox of water-insoluble, organic substrates with the molybdate/H2O2 system is difficult since it was assumed that none of the customary solvents is suitable for maintaining the disproportionation, catalyzed by molybdate, of H2O2 into water and 1O2. The use of molybdenum catalysts, however, also has other disadvantages. For example, as well as catalyzing the H2O2 disproportionation, they also catalyze other undesired oxidations of some substrates. Allyl alcohols, for example, cannot be effectively peroxidized with the molybdate/H2O2 system since this substance group is epoxidized by molybdenum in the presence of H2O2. A further disadvantage of these catalysts is the relatively low pH range in which they function. These catalysts can only be used in the basic range between pH 9 and pH 12; the use of this system is accordingly unsuitable for acidic conditions.

[0005] A further way of chemically generating 1O2 is, for example, the heating of triphenyl phosphite ozonide, which is obtained from triphenyl phosphite and ozone. However, as is described, for example, in J. Org. Chem., Vol. 67, No 8, 2002, page 2418, this method is only used for mechanism studies since triphenyl phosphite is an expensive and also hazardous chemical.

[0006] During the base-catalyzed disproportionation of peracids, further reactive compounds are formed as well as 1O2, which lead to by-products.

[0007] Accordingly, it was an object of the present invention to find a way of generating 1O2 while avoiding the above disadvantages.

[0008] Unexpectedly, this object was achieved by the use of ozone and an Sn(II) compound.

[0009] Accordingly, the present invention provides a process for generating 1O2, which comprises treating an Sn(II) salt of the formula

SnXn (I)

[0010] in which X is an anion from the group consisting of trifluoromethanesulfonate, acetate, formate, oxalate, lactate, malonate, malate, tartrate, citrate, orthophosphate, sulfate, chloride, perchlorate and n is 1 or 2, in an organic solvent at a temperature of from −80° C. to 20° C. with 1 to 2 mol of ozone per mole of tin compound, and using the 1O2 which forms directly for the oxidation of organic substrates which react with 1O2.

[0011] In the process according to the invention, 1O2 is generated by the reaction of an Sn(II) salt of the formula (I) with ozone.

[0012] In the formula (1), X is an anion from the group consisting of trifluoromethaneulfonate, acetate, formate, oxalate, lactate, malonate, malate, tartrate, citrate, orthophosphate, sulfate, chloride, perchlorate and n is 1 or 2 depending on the anion.

[0013] Preferred Sn(II) salts are tin(II) trifluoromethanesulfonate or tin(II) acetate.

[0014] The Sn(II) salt is dissolved in an organic solvent. Suitable solvents are ethyl acetate, butyl acetate, methanol, ethanol, dichloromethane or acetic acid. Preference is given to using ethyl acetate.

[0015] The mixture is then cooled to −80° C. to 20° C., preferably to −80° C. to −5° C., and ozone is introduced.

[0016] Ozone is added in the process according to the invention in an amount of from 1 to 2.0 mol per mole of Sn(II) salt. Preference is given to using one equivalent of ozone.

[0017] The 1O2 which forms is then used for the oxidation of organic substrates which react with 1O2.

[0018] This may take place according to the invention by metering in a solution of the corresponding substrate during the reaction of the Sn(II) salt with ozone. The metering preferably takes place continuously in this case.

[0019] Suitable solvents for the substrate here are, in turn, ethyl acetate, butyl acetate, methanol, ethanol, dichloromethane or acetic acid.

[0020] Preference is given to using ethyl acetate.

[0021] Preference is given to using the solvent which is also used for dissolving the Sn(II) salt.

[0022] Where necessary, excess ozone is then blown out, for example by flushing with argon or nitrogen, and the reaction solution which remains, which comprises the oxidation product, is worked up.

[0023] However, the substrate solution may also be added only after the Sn(II) salt has reacted with ozone and any excess ozone has finally been removed.

[0024] If the reaction of the Sn(II) salt with ozone takes place at relatively low temperatures (e.g. −80° C.), then the reaction solution treated with the substrate solution can optionally be heated, for example to −10° C.

[0025] The reaction solution which comprises the oxidation product is worked up by customary methods, such as, for example, extraction, drying and isolation of the oxidation product, for example by column chromatography.

[0026] As organic substrates which react with 1O2 it is possible to use the following compounds: olefins which contain one or more, i.e. up to 10, preferably up to 6, particularly preferably up to 4, C═C double bonds; electron-rich aromatics, such as C6-C50, preferably up to C30, particularly preferably up to C20, phenols, polyalkylbenzenes, polyalkoxybenzenes; polycyclic aromatics having 2 to 10, preferably up to 6, particularly preferably up to 4, aromatic rings; sulfides, such as, for example, alkyl sulfides, alkenyl sulfides, aryl sulfides which are either mono- or disubstituted on the sulfur atom, and also heterocycles with an 0, N or S atom in the ring, such as, for example, C4-C50, preferably up to C30, particularly preferably up to C20, furans, C4-C50, preferably up to C30, particularly preferably up to C20, pyrroles, C4-C60, preferably up to C30, particularly preferably up to C20, thiophenes. The substrates can here have one or more substituents, such as halogen (F, Cl, Br, J), cyanide, carbonyl groups, hydroxyl groups, C1-C50, preferably up to C30, particularly preferably up to C20, alkoxy groups, C1-C50, preferably up to C30, particularly preferably up to C20, alkyl groups, C6-C50, preferably up to C30, particularly preferably up to C20, aryl groups, C2-C50, preferably up to C30, particularly preferably up to C20, alkenyl groups, C2-C50, preferably up to C30, particularly preferably up to C20, alkynyl groups, carboxylic acid groups, ester groups, amide groups, amino groups, nitro groups, silyl groups, silyloxy groups, sulfone groups, sulfoxide groups. In addition, the substrates may be substituted by one or more NR1R2 radicals in which R1 or R2 may be identical or different and are H; C1-C50, preferably up to C30, particularly preferably up to C20, alkyl; formyl; C2-C50, preferably up to C30, particularly preferably up to C20, acyl; C7-C50, preferably up to C30, particularly preferably up to C20, benzoyl, where R1 and R2 can also together form a ring, such as, for example, in a phthalimido group.

[0027] Examples of suitable substrates are: 2-butene; isobutene; 2-methyl-1-butene; 2-hexene; 1,3-butadiene; 2,3-dimethylbutene; Δ9,10-octalin, 2-phthalimido-4-methyl-3-pentene; 2,3,-dimethyl-1,3-butadiene; 2,4-hexadiene; 2-chloro-4-methyl-3-pentene; 2-bromo-4-methyl-3-pentene; 1-trimethylsilylcyclohexene; 2,3-dimethyl-2-butenyl para-tolyl sulfone; 2,3-dimethyl-2-butenyl para-tolyl sulfoxide; N-cyclohexenyl-morpholine; 2-methyl-2-norbornene; terpinolene; α-pinene; β-pinene; β-citronellol; ocimene; citronellol; geraniol; farnesol; terpinene; limonene; trans-2,3-dimethylacrylic acid; α-terpinene; isoprene; cyclopentadiene; 1,4-diphenylbutadiene; 2-ethoxy-butadiene; 1,1′-dicyclohexenyl; cholesterol; ergosterol acetate; 5-chloro-1,3-cyclohexadiene; 3-methyl-2-buten-1-ol; 3,5,5-trimethylcyclohex-2-en-1-ol; phenol, 1,2,4-trimethoxybenzene, 2,3,6-trimethylphenol, 2,4,6-trimethylphenol, 1,4-dimethyl-naphthalene, furan, furfuryl alcohol, furfural, 2,5-dimethylfuran, isobenzofuran, dibenzyl sulfide, (2-methyl-5-tert-butyl)phenyl sulfide etc.

[0028] As a result of the oxidation according to the invention, the substrates produce the corresponding oxidation product. Alkenes, (polycyclic) aromatics or heteroaromatics give, in particular, hydroperoxides, peroxides, alcohols or ketones.

[0029] As a result of the process according to the invention, 1O2 is generated in a simple and efficient manner. A further advantage of the process is that no water is formed during the reaction.

EXAMPLE 1

Generation of Singlet Oxygen by Means of Ozone and Tin(II) trifluoromethanesulfonate at −80° C.

[0030] 1.52 g (4.1 mmol) of tin(II) trifluoromethanesulfonate were dissolved in 150 ml of ethyl acetate and cooled to −80° C. in a batch ozonolysis apparatus. One equivalent of ozone was added to this solution at −80° C. Excess ozone was then blown off by flushing the apparatus with argon. The tin ozonoid complex generated in this way was treated with 0.25 g (1.8 mmol) of α-terpinene in 10 ml of ethyl acetate and the reaction solution was warmed to −10° C. This solution was filtered with suction over a frit containing celite into a vacuum flask filled with a sodium chloride/ice mixture.

[0031] This mixture was warmed to room temperature and the organic phase was separated from the aqueous phase. The aqueous phase was extracted again with ethyl acetate. The combined organic fractions were washed with water and then dried with sodium sulfate. Sodium sulfate was filtered off and the resulting solution was evaporated down under reduced pressure.

[0032] The singlet oxidation product (Ascaridol) was isolated from the resulting yellow oil by means of column chromatography. For this purpose, 10 g of silica gel 60A were used as the stationary phase, and a 9:1 mixture of n-hexane:MTBE was used as the mobile phase.

[0033] The combined fractions which comprised Ascaridol were evaporated down, giving a yellow oil. The product was characterized by means of 1H-NMR and thin-layer chromatography.

[0034] Yield: 75 mg of Ascaridol (25% of theory).

EXAMPLE 2-5

Generation of Single Oxygen by Means of Ozone and Tin(II) Trifluoromethanesulfonate at −10° C.

[0035] 1 equivalent of tin(II) trifluoromethanesulfonate based on the substrate used in each case was dissolved in 150 ml of ethyl acetate and cooled to −10° C. in a batch ozonolysis apparatus. One equivalent of ozone was added to this solution at −10° C. During the ozonolysis, the amount of substrate given in the table and dissolved in 10 ml of ethyl acetate was continuously metered into the reaction solution by means of a perfusor pump. Excess ozone was then blown out by flushing the apparatus with argon. This solution was filtered with suction over a frit containing celite into a vacuum flask filled with a sodium chloride/ice mixture.

[0036] This mixture was heated to room temperature and the organic phase was separated off from the aqueous phase. The aqueous phase was extracted again with ethyl acetate. The combined organic fractions were washed with water and then dried with sodium sulfate. Sodium sulfate was filtered off and the solution obtained was evaporated down under reduced pressure.

[0037] The product was characterized and quantified by means of 1H-NMR, HPLC and thin-layer chromatography. The results are summarized in the table below.

1AmountusedConver-YieldEx. No.Substrate[mg]sion [%][%]Product2

16399.672.3

123.590.926.5

81.795.62.9

87.698.724.2|5.2

Singlet oxygen oxidation of organic substrates

Information

Publication Number

Date Filed

Date Published

Inventors

CPC

US Classifications

International Classifications

Abstract

Description

Claims

Priority Claims (1)