METHOD FOR PRODUCING DITHINE TETRACARBOXIMIDES

Information

  • Patent Application
  • 20140256956
  • Publication Number
    20140256956
  • Date Filed
    October 10, 2012
    12 years ago
  • Date Published
    September 11, 2014
    10 years ago
Abstract
The present invention relates to a new process for preparing dithiine-tetracarboximides.
Description

The present invention relates to a new process for preparing dithiine-tetracarboximides.


Dithiine-tetracarboximides as such are already known. It is also known that these dithiine-tetracarboximides can be used as anthelmintics against internal parasites of animals, more particularly nematodes, and have insecticidal activity (cf. U.S. Pat. No. 3,364,229). It is known, furthermore, that certain dithiine-tetracarboximides possess antibacterial activity and have a certain activity against causative organisms of human mycoses (cf. Il Farmaco 2005, 60, 944-947). It is also known that dithiine-tetracarboximides can be used as pigments in electrophotographic photoreceptors or as dyes in paints and polymers (cf. JP-A 10-251265, PL-B 143804).


Dithiine-tetracarboximides of the formula (I)




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in which

    • R1 and R2 are identical or different and are hydrogen, or are C1-C8-alkyl which is optionally substituted one or more times by halogen, —OR3, and/or —COR4, are C3-C7-cycloalkyl which is optionally substituted one or more times by halogen, C1-C4-alkyl or C1-C4-haloalkyl, or are aryl or aryl-(C1-C4-alkyl) each of which is optionally substituted one or more times by halogen, C1-C4-alkyl, C1-C4-haloalkyl, —COR4 or sulphonylamino,
    • R3 is hydrogen, C1-C4-alkyl or C1-C4-alkylcarbonyl or is aryl which is optionally substituted one or more times by halogen, C1-C4-alkyl or C1-C4-haloalkyl,
    • R4 is hydroxyl, C1-C4-alkyl or C1-C4-alkoxy,


      can be prepared in a variety of known ways.


For example, in one process (cf. U.S. Pat. No. 3,364,229; Chem. Ber. 1967, 100, 1559-1570), in a first stage, dichloromaleic anhydride of the formula (II) is reacted with an amine of the formula (III), optionally in the presence of a diluent. Subsequently, the resultant dichloromaleimides of the formula (IV) are then reacted with a sulphur compound (e.g. hydrogen sulphide or thiourea). The preparation of the dithiine-tetracarboximides of the formula (I) by this process can be illustrated by the following scheme:




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This process has the disadvantage that, for example, operating with the highly toxic gaseous hydrogen sulphide is from a technical standpoint very difficult, costly and inconvenient. When thiourea is used, unwanted by-products are obtained along with the target product, and are very difficult to remove, and detract from the attainable yields (cf. J. Heterocycl. Chem. 1988, 25, 901-906).


In another process which has been disclosed (cf. Synthetic Communications 2006, 36, 3591-3597), in a first stage, succinic anhydride of the formula (V) is reacted with an amine of the formula (III), optionally in the presence of a diluent. Subsequently, the resultant succinic monoamides of the formula (VI) are reacted for 6 hours with a large excess of thionyl chloride in the presence of dioxane as diluent, at room temperature, to give, finally, in a sequence of numerous reaction steps, the dithiine-tetracarboximides of the formula (I). The dithiine-tetracarboximides are optionally isolated directly from the reaction mixture or by filtration following addition of water. Depending on reaction conditions (diluents) and the nature of the radicals R, it is possible in certain circumstances to isolate the dithiine-diisoimides of the formula (VII) before they are converted into the dithiine-tetracarboximides of the formula (I). This preparation method for the dithiine-tetracarboximides of the formula (I) can be illustrated by the following scheme:




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Disadvantages of this process are the long reaction time and also the outcome where either the yields obtained generally do not exceed about 30-40% of theory or else the purities of the isolated products are inadequate (see comparative examples). A further disadvantage, in the case of aqueous work-up of the reaction mixture, is that it involves destroying large amounts of thionyl chloride; the gases formed (SO2 and HCl) have to be disposed of. Likewise a disadvantage is the fact that, from experience (see comparative examples), the product is not obtained in one fraction. Instead, it is frequently the case that, following initial isolation of product by filtration, further product precipitates from the filtrate after prolonged standing (overnight, for example), and must be isolated again by filtration. Occasionally this operation must be carried out once more. This procedure is very laborious and time-consuming.


It is known, moreover, that dithiine-tetracarboximides are obtained by dissolving N-substituted succinamides in dry 1,4-dioxane and then adding thionyl chloride to the solution. The reaction mixture is subsequently heated and the solution is concentrated in vacuo and, via column chromatography, is separated and purified (cf. J. Heterocycl. Chem. 2010, 47, 188-193).


Consequently there continues to be a need for a technically simple and economic preparation process for dithiine-tetracarboximides of the formula (I).


A new process has been found for preparing dithiine-tetracarboximides of the general formula (I)




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in which R1 and R2 have the definitions indicated above,


characterized in that


in a first stage, succinic monoamide carboxylates of the formula (VI)




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in which R is R1 or R2,

    • M is a cation selected from the group consisting of alkali metals, alkaline earth metals, transition metals and metals, and
    • m is 1, 2, 3, or 4,


      are reacted with an excess of thionyl chloride, optionally in the presence of a diluent,


      then the excess of thionyl chloride is removed and the resulting product mixture is converted in a second stage, in an organic solvent, into the dithiine-tetracarboximides of the formula (I).


In this way the dithiine-tetracarboximides of the formula (I) can be obtained in relatively high yield, a relatively short time, and relatively good purity.


The product mixture obtained in the first step of the process of the invention also already includes dithiine-tetracarboximides of the formula (I), but its principal components are polysulphides of the formula (IX),




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and also, depending on the work-up method, thiosulphonic acid derivatives of the formula (VIII)




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The thiosulphonic acid derivatives of the general formula (VIII) and the polysulphides of the general formula (IX) are new and are likewise provided by the present invention.


In the thiosulphonic acid derivatives of the general formula (VIII), R stands for the definitions of R1 and R2, indicated above, and X stands for chlorine or hydroxyl.


In the polysulphides of the general formula (IX), R1 and R2 stand for the definitions indicated above, and n stands for 0, 1, 2, 3, 4, 5, 6, 7 or 8.


Compounds of the general formula (VIII) are obtained, alongside other products, when the reaction mixture, following the reaction of the compounds of the general formula (VI) with thionyl chloride, is concentrated.


Compounds of the general formula (IX) are obtained, alongside other products, when the reaction mixture, following the reaction of the compounds of the general formula (VI) with thionyl chloride, is concentrated, dissolved in an inert, water-immiscible solvent such as methylene chloride, for example, and extracted by shaking with water at room temperature. Following removal of the organic phase, drying and concentrating, a mixture is obtained which in addition to dithiine-tetracarboximides of the formula (I) contains primarily compounds of the general formula (IX).







The process of the invention for preparing the dithiine-tetracarboximides of the formula (I) can be illustrated by the following scheme:




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A general definition of the succinic monoamide carboxylates used as starting materials when carrying out the process of the invention is provided by the formula (VI). R stands for the definitions of R1 or R2.

    • R1 and R2 preferably are identical or different and preferably are hydrogen, or are C1-C6-alkyl which is optionally substituted one or more times by fluorine, chlorine, bromine, —OR3 and/or —COR4, or are C3-C7-cycloalkyl which is optionally substituted one or more times by chlorine, methyl or trifluoromethyl, or are phenyl or phenyl-(C1-C4-alkyl) each of which is optionally substituted one or more times by fluorine, chlorine, bromine, methyl, trifluoromethyl, —COR4 and/or sulphonylamino.
    • R1 and R2 more preferably are identical or different and more preferably are hydrogen, or are C1-C4-alkyl which is optionally substituted one or more times by fluorine, chlorine, hydroxyl, methoxy, ethoxy, methylcarbonyloxy and/or carboxyl, or are C3-C7-cycloalkyl which is optionally substituted one or more times by chlorine, methyl or trifluoromethyl, or are phenyl, benzyl, 1-phenethyl, 2-phenethyl or 2-methyl-2-phenethyl each of which is optionally substituted one to three times by fluorine, chlorine, bromine, methyl, trifluoromethyl, —COR4 and/or sulphonylamino.
    • R1 and R2 very preferably are identical or different and very preferably are hydrogen, methyl, ethyl, n-propyl, isopropyl, 2,2-difluoroethyl or 2,2,2-trifluoroethyl or are cyclopropyl or cyclohexyl each of which is optionally substituted by chlorine, methyl or trifluoromethyl.
    • R1 and R2 more particularly preferably are simultaneously methyl.
    • R3 preferably is hydrogen, methyl, ethyl, methylcarbonyl or ethylcarbonyl or is phenyl which is optionally substituted one or more times by fluorine, chlorine, methyl, ethyl, n-propyl, isopropyl or trifluoromethyl.
    • R3 more preferably is hydrogen, methyl, methylcarbonyl or phenyl.
    • R4 preferably is hydroxyl, methyl, ethyl, methoxy or ethoxy.
    • R4 more preferably is hydroxyl or methoxy.
    • M preferably is Li, Na, K, Rb or Cs with
    • m as 1,
      • or
      • Be, Mg, Ca, Sr or Ba, with
    • m as 2,
    • or
      • Ti, V, Mn, Fe, Co, Ni, Cu, Zn, Al with
    • m as 1, 2, 3 or 4.
    • M more preferably is Li, Na, K, with
    • m as 1,
    • or
      • Be, Mg, Ca, with
    • m as 2,
    • or
      • Mn, Fe, Co, Al with
    • m as 1, 2, 3 or 4.
    • M very preferably is Na, K, with
    • m as 1,
    • or
      • Mg, Ca, with
    • m as 2,
    • or
      • Mn, Fe, Al with
    • m as 2, 3 or 4.


As starting material it is particularly preferred to use N-methylsuccinamide carboxylates, giving as the end product the compound (I-1) 2,6-dimethyl-1H,5H-[1,4]dithiino[2,3-c:5,6-c′]dipyrrole-1,3,5,7(2H,6H)-tetrone.


If sodium N-tert-butylsuccinamide carboxylate is used as starting material, the end product obtained is the compound (I-2) 2,6-di-tert-butyl-1H,5H-[1,4]dithiino[2,3-c:5,6c′]dipyrrole-1,3,5,7(2H,6H)-tetrone.


If sodium N-cyclohexylsuccinamide carboxylate is used as starting material, the end product obtained is the compound (I-3) 2,6-dicyclohexyl-1H,5H-[1,4]dithiino[2,3-c:5,6-c′]dipyrrole-1,3,5,7(2H,6H)-tetrone.


If sodium N-propylsuccinamide carboxylate is used as starting material, the end product obtained is the compound (I-4) 2,6-dipropyl-1H,5H-[1,4]dithiino[2,3-c:5,6-c′]dipyrrole-1,3,5,7(2H,6H)-tetrone.


Intermediates obtained with particular preference are


(VIII-I) S-(4-chloro-1-methyl-2,5-dioxo-2,5-dihydro-1H-pyrrol-3-yl) chlorothiosulphate (R=Me, X=Cl),


(IX-1) 3,3′-trisulphane-1,3-diylbis(4-chloro-1-methyl-1H-pyrrole-2,5-dione) (R1=R2=Me, n=1)


(IX-2) 3,3′-disulphanediylbis(4-chloro-1 -methyl-1H-pyrrole-2,5-dione) (R1=R2=Me, n=0)


(IX-3) 3,3′-disulphanediylbis(1-tert-butyl-4-chloro-1H-pyrrole-2,5-dione) (R1=R2=t-Bu, n=0)


(IX-4) 3,3′-trisulphane-1,3-diylbis(1-tert-butyl-4-chloro-1H-pyrrole-2,5-dione) (R1=R2=t-Bu, n=1)


(IX-5) 3,3′-trisulphane-1,3-diylbis(4-chloro-1-cyclohexyl-1H-pyrrole-2,5-dione) (R1=R2=cyclohexyl, n=1)


The amount of thionyl chloride in the first step of the process of the invention is between 1 and 100 mol per mole of succinic monoamide carboxylate of the formula (VI). It is preferred to use between 2 and 50 mol, more preferably amounts of between 4 and 40 mol, per mole of succinic monoamide carboxylate of the formula (VI).


The reaction temperature in the first step of the process of the invention can be varied within wide limits and is between 0° C. and 150° C. In order to obtain satisfactory space-time yields, it is preferred to operate at temperatures between 20° C. and 120° C., more preferably between 30° C. and 100° C.


The reaction time in the first step of the process of the invention is between 10 minutes and 24 hours. It is preferred to operate for between 30 minutes and 6 hours, more preferably between 1 and 4 hours.


The first step of the process of the invention can be carried out optionally in the presence of a diluent which as far as possible is inert under the reaction conditions. Such diluents include, by way of example, aliphatic hydrocarbons such as pentane, hexane, heptane, cyclohexane, methylcyclohexane, chlorinated hydrocarbons such as methylene chloride, chloroform, 1,2-dichloroethane, aromatic hydrocarbons such as toluene, xylene, mesitylene, chlorinated aromatic hydrocarbons such as chlorobenzene, dichlorobenzene, ethers such as diethyl ether, methyl tert-butyl ether, tetrahydrofuran, dioxane, nitriles such as acetonitrile, propionitrile, butyronitrile, esters such as methyl acetate and ethyl acetate. It is preferred to operate in methylene chloride, chloroform or 1,2-dichloroethane or without diluent.


The thionyl chloride can be removed in principle by hydrolysis with water. The thionyl chloride is removed preferably by distillation under reduced pressure.


The diluent optionally present is preferably likewise distilled off under reduced pressure.


In the second step of the process of the invention, the residue that is obtained following removal of the excess thionyl chloride and optionally of the diluent is dissolved in a new diluent and, by heating in this solvent, is converted into the dithiine-carboximides of the formula (I). The reaction mixture is preferably stirred during this procedure.


In the second step of the process of the invention, organic solvents or solvent mixtures are used.


Suitable diluents for the second step of the process of the invention include, specifically, water, dimethyl sulphoxide, sulpholane, alcohols such as, for example, methanol, ethanol, propanol, isopropanol, 1-butanol, 2-butanol, isobutanol, tertiary-butanol, 1-pentanol, cyclopentanol, cyclohexanol, ethylene glycol, ethylene glycol monomethyl ether, hydrocarbons such as hexane, heptane, cyclohexane, methylcyclohexane, toluene, xylenes, mesitylene, ethylbenzene, cumene, chlorobenzene, dichlorobenzene, nitrobenzene, esters such as methyl acetate, ethyl acetate, amides such as formamide, N,N-dimethylformamide; N,N-dimethylacetamide, N-methylpyrrolidone, ethers such as methyl tert-butyl ether, tetrahydrofuran, 1,4-dioxane, nitriles such as acetonitrile, propionitrile, butyronitrile, benzonitrile, ketones such as acetone, methyl ethyl ketone, methyl isobutyl ketone, pinacolone, carboxylic acids such as formic acid, acetic acid, propionic acid, or mixtures of these diluents.


Preference is given to using water, dimethyl sulphoxide, methanol, ethanol, propanol, isopropanol, 1-butanol, 2-butanol, isobutanol, tertiary-butanol, 1-pentanol, cyclohexanol, ethylene glycol, methyl acetate, N,N-dimethylformamide; N,N-dimethylacetamide, tetrahydrofuran, 1,4-dioxane, acetonitrile, acetone, methyl ethyl ketone, methyl isobutyl ketone, acetic acid or mixtures of these diluents.


Very particular preference is given to using mixtures of water and methanol, ethanol, propanol, isopropanol, 1-butanol, 2-butanol, isobutanol, 1-pentanol, methyl acetate, tetrahydrofuran, 1,4-dioxane, acetonitrile, acetone, acetic acid.


The mixing ratio of water to organic solvent here may be varied within wide limits of, for example, 9:1 to 1:9.


The reaction temperature in the second step of the process of the invention can be varied within wide limits and is between 0° C. and 200° C. It is preferred to operate at temperatures between 20° C. and 150° C., more preferably between 30° C. and 130° C.


The reaction time in the second step of the process of the invention is between 5 minutes and 24 hours. It is preferred to operate for between 30 minutes and 12 hours, more preferably between 1 and 6 hours.


The present invention also provides processes for preparing polysulphides of the formula (IX)




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in which

    • R1 and R2 are identical or different and are hydrogen, or are C1-C8-alkyl which is optionally substituted one or more times by halogen, —OR3, and/or —COR4, are C3-C7-cycloalkyl which is optionally substituted one or more times by halogen, C1-C4-alkyl or C1-C4-haloalkyl, or are aryl or aryl-(C1-C4-alkyl) each of which is optionally substituted one or more times by halogen, C1-C4-alkyl, C1-C4-haloalkyl, —COR4 or sulphonylamino,
    • R3 is hydrogen, C1-C4-alkyl or C1-C4-alkylcarbonyl or is aryl which is optionally substituted one or more times by halogen, C1-C4-alkyl or C1-C4-haloalkyl,
    • R4 is hydroxyl, C1-C4-alkyl or C1-C4-alkoxy,
    • n is 0, 1 or 2,


      and also for preparing thiosulphonic acid derivatives of the formula (VIII)




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in which R is R1 or R2 and X is chlorine or hydroxyl,


characterized in that


in a first stage succinic monoamides of the formula (VI)




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in which R is R1 or R2,


and

    • M is a cation selected from the group consisting of alkali metals, alkaline earth metals, transition metals and metals, and
    • m is 1, 2, 3 or 4,


      with an excess of thionyl chloride, optionally in the presence of a diluent.

Claims
  • 1. Process for preparing a dithiine-tetracarboximide of formula (I)
  • 2. Process according to claim 1, wherein in the first stage from 2 to 100 mol of thionyl chloride are used per mole of succinic monoamide of formula (VI).
  • 3. Process according to claim 1, wherein in the first stage a succinic monoamide carboxylate of formula (VI)
  • 4. Process according to claim 1, wherein in the first stage a succinic monoamide carboxylate of formula (VI)
  • 5. Process according to claim 1, wherein in the first stage a succinic monoamide carboxylate of formula (VI)
  • 6. Process according to claim 1, wherein the first stage step is carried out without diluent.
  • 7. Process according to claim 1, wherein in the second stage an organic solvent is used which is at least partly miscible with water.
  • 8. Process according to claim 1, wherein solvent used in the second stage comprises one or more of water, dimethyl sulphoxide, sulpholane, alcohols optionally comprising methanol, ethanol, propanol, isopropanol, 1-butanol, 2-butanol, isobutanol, tertiary-butanol, 1-pentanol, cyclopentanol, cyclohexanol, ethylene glycol, ethylene glycol monomethyl ether, hydrocarbons such as hexane, heptane, cyclohexane, methylcyclohexane, toluene, xylenes, mesitylene, chlorobenzene, dichlorobenzene, nitrobenzene, esters optionally comprising methyl acetate, ethyl acetate, amides optionally comprising formamide, N,N-dimethylformamide; N,N-dimethylacetamide, N-methylpyrrolidone, ethers such as methyl tert-butyl ether, tetrahydrofuran, 1,4-dioxane, nitriles optionally comprising acetonitrile, propionitrile, butyronitrile, benzonitrile, ketones such as optionally comprising acetone, methyl ethyl ketone, methyl isobutyl ketone, pinacolone, carboxylic acids such as formic acid, acetic acid, propionic acid, and/or a mixture thereof these diluents.
  • 9. Process according to claim 1, wherein the second stage is carried out at a temperature from 20° C. to 150° C.
  • 10. Process for preparing a polysulphide of formula (IX),
Priority Claims (1)
Number Date Country Kind
11185004.6 Oct 2011 EP regional
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/EP2012/070104 10/10/2012 WO 00 4/10/2014