WO2013173020A1 - Isosorbide and isomannide derivatives and processes for making the same - Google Patents

Isosorbide and isomannide derivatives and processes for making the same Download PDF

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Publication number
WO2013173020A1
WO2013173020A1 PCT/US2013/037098 US2013037098W WO2013173020A1 WO 2013173020 A1 WO2013173020 A1 WO 2013173020A1 US 2013037098 W US2013037098 W US 2013037098W WO 2013173020 A1 WO2013173020 A1 WO 2013173020A1
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Prior art keywords
isosorbide
isoidide
isomannide
furan
dicarboxylic acid
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PCT/US2013/037098
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French (fr)
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Kenneth F. STENSRUD
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Archer Daniels Midland Company
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D493/00Heterocyclic compounds containing oxygen atoms as the only ring hetero atoms in the condensed system
    • C07D493/02Heterocyclic compounds containing oxygen atoms as the only ring hetero atoms in the condensed system in which the condensed system contains two hetero rings
    • C07D493/04Ortho-condensed systems

Definitions

  • compositions incorporating these monomers are disclosed.
  • Terephthalic acid (benzene- 1 ,4 ⁇ dicarboxylic acid) is a cyclic bifunctional carboxylic acid monomer which finds widespread commercial application as a primary precursor of polyethylene terephthalate (PET), a thermoplastic resin with widespread use in textiles and containers for food, beverages, and other liquids, Terephthafic acid is polymerized, usually with ethylene glycol monomers in an equimolar ratio with terephthalic acid, to yield the polycondensate PET.
  • PET polyethylene terephthalate
  • Terephthafic acid is polymerized, usually with ethylene glycol monomers in an equimolar ratio with terephthalic acid, to yield the polycondensate PET.
  • Terephthalic acid can also be copolymerized with other diacid monomers or esters thereof to obtain polymers with specific desired properties.
  • Terephthalic acid is commonly produced by oxidation of p ⁇ xylene originating from non ⁇ renewable petroleum derivatives.
  • petroleum-derived materials are frequently expensive to produce and use because of fluctuations in the pricing and availability of petroleum, and are increasingly likely to remain so as petroleum reserves are reduced and new supplies prove more costly and difficult to secure.
  • PET polymers have raised concerns for their potential to disrupt human endocrine activity, as it has been suggested that PET polymers may release yield endocrine disrupters under commonly used conditions.
  • PET may under certain conditions break down to yield acetaldehyde, causing the development of off ⁇ taste in bottled water.
  • Detectable levels of antimony catalyst are present both inside PEC polymers and on the surface, and can migrate into food and beverages in contact with PET, especially fruit juices in PET bottles.
  • carbohydrates are however generally unsuited to current high temperature industrial processes. Compared to petroleum-based, hydrophobic aliphatic or aromatic feedstocks with a low degree of functionalization, carbohydrates such as polysaccharides are complex, overfunctionalized hydrophilic materials.
  • isosorbide and the related isohexides isomannide and isoidide are especially of interest.
  • the diacid was expected to be a possible biobased alternative to terephthalic acid, initial efforts from theDNile then focused on hydrolysis to the diacid.
  • Various aqueous routes were explored but also proved unsatisfactory; finally it was determined that by making the dinitrile into a dimethyl ester, then purifying the same, the purified dimethyl ester could undergo hydrolysis to provide isoidide dicarboxylic acid.
  • the diacid is described as having been obtained as "a white solid in high isolated yield (84%) and high purity (99.0%).”
  • Other bifunctional derivatives were then also prepared from the isoidide dimethyl ester, in particular, a diol and a diamine.
  • the present invention in a first aspect concerns isomannide-3,6- dicarboxylic acid.
  • the invention in a second aspect, relates to isosorbide-3,6- dicarboxylic acid.
  • lsomannide-3,6-dicarboxylic acid was successfully prepared from isoidide through isoidide ditriflate and through cyanide displacement to the dinitrile of isomannide (including a Walden inversion from an exo-exo stereochemistry to an endo-endo configuration), followed by hydrolysis of the cyanide to the dicarboxylic acid [lUPAC (3S, 3aS, 6S, 6aS)- hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid]. Details of the synthesis and isolation are reported below in Example 1.
  • the starting isoidide material can be obtained by any known method for making isoidide.
  • the isoidide starting material can be prepared by epimerization from isosorbide.
  • epimerization is induced by means of Ni catalysis, using nickel supported on diatomaceous earth.
  • the reaction is conducted under relatively severe conditions, such as a temperature of 220°C to 240 °C at a pressure of 150 atmosphere.
  • the reaction reaches a steady state after two hours, with an equilibrium mixture containing isoidide (57%), isosorbide (36%) and
  • L-iditol is prepared starting from sorbitol.
  • sorbitol is converted by fermentation into L-sorbose, which is subsequently hydrogenated into a mixture of D-sorbitol and L-iditol. This mixture is then converted into a mixture of L-iditol and L-sorbose. After separation from the L-sorbose, the L-iditol can be converted into isoidide.
  • sorbitol is converted into isoidide in a four-step reaction, in a yield of about 50%.
  • a preferred method for preparing isoidide by the epimerization of isosorbide is described in European Patent Application No. 12156170.8, filed Feb. 20, 2012 for "Method of Making Isoidide". wherein a supported ruthenium catalyst is used at a starting pH of above 7, preferably of from 8 to 10, with the starting pH referring to the pH of the aqueous solution of isosorbide.
  • the support can vary widely, including silica, alumina, titania, zirconia, and carbon.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports.
  • a carbon support is preferred
  • the catalytically active metal preferably consists essentially of ruthenium, and the support preferably consists essentially of carbon.
  • a suitable ruthenium content is described as from 1% to 10% by weight of ruthenium, based on the total weight of the catalyst, preferably being about 5% by weight of the catalyst.
  • the isosorbide concentration is in a range of from 25% by weight to 75% by weight. More preferably, the isosorbide concentration is 30% to 60% by weight- The optimum concentration is believed to approximately 50% by weight.
  • the aqueous solution is subjected to an atmosphere comprising hydrogen.
  • the hydrogen pressure can widely vary, for example, from 20 to 200 bars. However, it was found particularly effective to employ a relatively low pressure in the range of from to 55 bars, and preferably about 40 bars.
  • the catalyst concentration in the reactor calculated as a weight percentage based on the aqueous solution of isosorbide, can range from as low as, e.g., 1% to as high as, e.g. 50%.
  • a 5% ruthenium catalyst is preferred for a concentration of from 2 to 20%, and more preferably about 4%. it will be understood that these percentages will hold, mutatis mutandis, for other water paste concentrations than 50%, and other catalyst loadings than 5%.
  • the ruthenium catalyst as mentioned preferably comprises a carbon support.
  • carbon support e.g. activated carbon or carbon nanotubes.
  • the activated carbon can be, e.g., 50-70% wetted powder.
  • preferred catalysts include commercial ruthenium on carbon catalysts ex BASF or Evonik (Strem
  • Ru/C catalysts A background reference on Ru/C catalysts is Sifontes Herrera et al, J. Chem Technol Biotechnol (2011), "Sugar hydrogenation over a Ru/C catalyst.”
  • the epimerization reaction is conducted preferably at an elevated temperature, i.e. above 20°C, and preferably below 250°.
  • a preferred temperature range is 200° to 240°, most preferably about 220°C.
  • the duration of the reaction will generally be shorter at higher temperatures.
  • the residence time in the reactor where the isosorbide solution is subjected to hydrogen under the influence of the catalyst will generally range from 0.1 to 10 hours, preferably. 0.25 to 4 hours, and more preferably 1-2 hours.
  • the isoidide starting material can be recovered by separation methods known to the skilled person, such as by chromatographic techniques, selective crystallization or distillation.
  • the latter can be conducted, e.g. as disclosed by Wright et al., J. Org. Chem., 1964, 29 (10), pp 2979-2982, mentioned above.
  • isosorbide-3,6 ⁇ dicarboxylic acid was also successfully prepared from isosorbide, according to the procedure described in Example 2 below.
  • the isosorbide starting material can be obtained by any known method for making isosorbide, for example, as described in US
  • the slightly darkened solution was poured over 50 mL of ice water, 50 ml of methylene chloride was added, and the resultant Diphasic solution was transferred to a 250 mL separatory funnel.
  • the bottom organic phase was removed, washed twice with 50 mL of water, and concentrated in vacuo to produce 8.10 g of a dark, seemingly insoluble precipitate.
  • Approximately 2 g of this material was triturated with 100 mL of dichloromethane for 1 hour, the solids were filtered off, and the solution concentrated in vacuo, producing about 1.600 g of a crude, light- yellow semisolid.
  • This material was then dissolved in a minimum amount of methylene chloride, adsorbed to about 20 g of silica gel (60A, 40-63 ⁇ , 230 x 400 mesh), dried under vacuum, and added to a prefabricated silica gel column.
  • Hexane (Hex)/Ethyl Acetate (EtOAc) mobile phase proportion monitoring the elution of products by GC/MS (CI) and TLC (cerium molybdate stain).
  • the initial products (diastereomers) eluted as 20 cc fractions at 1 :1 Hex/EtOAc with a rf of -0.6 (1:1 Hex/EtOAc). After concentration, 130 mg of a clear semi-solid was obtained.
  • High resolution (HR) GC/MS revealed signals at 14.00 min and 15.28 min and manifested the same mass spectra
  • (3R,3aR,6S,6aR)-hexahydrofuro[3,2-b]furan-3,6-dicarbonitrile and enantiomer is calculated to be about 400 mg (23%) and that of the 3R,3aR,6R,6aR)- hexahydrofuro[3,2-b]furan-3,6-dicarbonitrile to be about 480 mg (27%).
  • the isomannide 3.6- dicarboxylic ((35, 3aS, 6S, 6aS)-hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid) was prepared from the dinitrile:
  • a 100 ml, two neck boiling flask containing a magnetic stir bar was charged with 1.00 g of isosorbide (6.84 mmol), 4.25 g of triflic anhydride (15.05 mmol), and 30 mL of anhydrous THF.
  • An argon inlet adapter and rubber septum were then fitted to the flask ports, and the mixture was chilled to about 0 deg. C in an ice/brine bath.
  • 1.65 mL of pyridine (20.5 mmol) was injected dropwise via a syringe over a 5 minute period.
  • isosorbide ditriflate (2.44 mmol) was dissolved in 10 mL of THF, then the solution was poured into a 50 mL addition funnel and added to the cyanide solution at a rate of -2 mL/min. Once the entire volume had been added, the mixture was removed from the ice/brine bath and the reaction continued at room temperature for another 2 hours. At this time, a deep red solution was observed, and multiple spots developed on a silica gel TLC plate. The solvent was evaporated under vacuum, the remainder dissolved in a minimum amount of CH2CI2 and charged to a prefabricated silica gel column. Carefully monitored flash chromatography was then conducted with gradient CH2CI2 to EtOAc eluents. Three distinct fraction sets were collected; those
  • the isosorbide 3,6-diacid was made (lUPAC (3R,3aR,6S,6aR)- hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid, corresponding to structure 4).

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  • Organic Chemistry (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)

Abstract

The dicarboxylic acids of isomannide and isosorbide are disclosed, with processes for making the same.

Description

ISOSORBIDE AND ISOMANN1DE DERIVATIVES AND PROCESSES
FOR MAKING THE SAME
[0001]The present application is in the field of art relating to cyclic bifunctional carboxylic acid monomers derived from renewable materials, to the methods by which such monomers are made, and to polymer
compositions incorporating these monomers.
[0002] Terephthalic acid (benzene- 1 ,4~dicarboxylic acid) is a cyclic bifunctional carboxylic acid monomer which finds widespread commercial application as a primary precursor of polyethylene terephthalate (PET), a thermoplastic resin with widespread use in textiles and containers for food, beverages, and other liquids, Terephthafic acid is polymerized, usually with ethylene glycol monomers in an equimolar ratio with terephthalic acid, to yield the polycondensate PET. Terephthalic acid can also be copolymerized with other diacid monomers or esters thereof to obtain polymers with specific desired properties.
[0003] Terephthalic acid is commonly produced by oxidation of p~ xylene originating from non~renewable petroleum derivatives. However, such petroleum-derived materials are frequently expensive to produce and use because of fluctuations in the pricing and availability of petroleum, and are increasingly likely to remain so as petroleum reserves are reduced and new supplies prove more costly and difficult to secure. Further, PET polymers have raised concerns for their potential to disrupt human endocrine activity, as it has been suggested that PET polymers may release yield endocrine disrupters under commonly used conditions. In addition, PET may under certain conditions break down to yield acetaldehyde, causing the development of off~taste in bottled water. Detectable levels of antimony catalyst are present both inside PEC polymers and on the surface, and can migrate into food and beverages in contact with PET, especially fruit juices in PET bottles.
[0004] In view of the dependence of conventional PET polymers on increasingly scarce and costly petroleum resources and further in view of the additional concerns just described, renewable source~based alternatives have been earnestly sought. The most abundant type of biobased or renewable source alternative feedstock for producing such materials, namely
carbohydrates, are however generally unsuited to current high temperature industrial processes. Compared to petroleum-based, hydrophobic aliphatic or aromatic feedstocks with a low degree of functionalization, carbohydrates such as polysaccharides are complex, overfunctionalized hydrophilic materials.
[0005} Consequently, researchers have sought to produce biobased materials that derive from carbohydrates but which are less highly
functionalized, including more stable bifunctional materials more or less analogous to terephthalic acid, such as 2,5~furandicarboxylic acid (FDCA). levulinic acid and isosorbide. For the present invention, isosorbide and the related isohexides isomannide and isoidide are especially of interest.
Recently, in Wu et al., "Isohexide Derivatives from Renewable Resources as Chiral Building Blocks", ChemSusChem, vol. 4, pp. 599~603 (2011), several C2/C5 carbon-extended bifunctional derivatives were synthesized from isomannide to provide greater reactivity in common melt polycondensation conditions for forming polyester polymers using the isohexides (or derivatives based thereon). The initial strategy was to make the dinitrile by a
nucleophilic substitution of activated hydroxyl groups by cyanide.
Unexpectedly for the authors, however, neither the bistosylate nor
bismesylate of isomannide showed any reactivity towards cyanide, even though a broad range of reaction conditions were tried. Finally, a successful combination was tried, and the authors were able to obtain the desired dinitrile (in an exo~exo stereochemistry compared to the original endo~endo
stereochemistry of the isomannide starting material) through the bistriflate of isomannide, formed by reacting isomannide with trifluorosulfonic anhydride and pyridine in dichloromethane.
[0006] Since the diacid was expected to be a possible biobased alternative to terephthalic acid, initial efforts from the dintrile then focused on hydrolysis to the diacid. Various aqueous routes were explored but also proved unsatisfactory; finally it was determined that by making the dinitrile into a dimethyl ester, then purifying the same, the purified dimethyl ester could undergo hydrolysis to provide isoidide dicarboxylic acid. The diacid is described as having been obtained as "a white solid in high isolated yield (84%) and high purity (99.0%)." Other bifunctional derivatives were then also prepared from the isoidide dimethyl ester, in particular, a diol and a diamine.
[0007] While the isoidide diacid and other bifunctional derivatives of isoidide were thus eventually successfully made starting from isomannide, the article does also mention the possibility of the like bifunctional derivatives being made starting from the isosorbide and isoidide stereoisomers; but in contemplating this possibility, the authors noted that Sn2 reactions on isohexide endo-hydroxyl groups were strongly favored over exo-substitution for steric reasons, and so the authors selected the endo-endo isomannide isomer as a starting material for trying to make the novel bifunctional derivatives in question. The exo-endo isosorbide and exo-exo isoidide derivatives were carried over in the meanwhile for further "investigations."
SUMMARY OF THE INVENTION
[0008]The present invention in a first aspect concerns isomannide-3,6- dicarboxylic acid. In a second aspect, the invention relates to isosorbide-3,6- dicarboxylic acid.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
[0009] lsomannide-3,6-dicarboxylic acid was successfully prepared from isoidide through isoidide ditriflate and through cyanide displacement to the dinitrile of isomannide (including a Walden inversion from an exo-exo stereochemistry to an endo-endo configuration), followed by hydrolysis of the cyanide to the dicarboxylic acid [lUPAC (3S, 3aS, 6S, 6aS)- hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid]. Details of the synthesis and isolation are reported below in Example 1.
[0010] The starting isoidide material can be obtained by any known method for making isoidide. According to one embodiment, the isoidide starting material can be prepared by epimerization from isosorbide. In L. W. Wright, J. D. Brandner, J. Org. Chem., 1964, 29 (10), pp 2979-2982, for example, epimerization is induced by means of Ni catalysis, using nickel supported on diatomaceous earth. The reaction is conducted under relatively severe conditions, such as a temperature of 220°C to 240 °C at a pressure of 150 atmosphere. The reaction reaches a steady state after two hours, with an equilibrium mixture containing isoidide (57%), isosorbide (36%) and
isomannide (7%). Comparable results were obtained when starting from isoidide or isomannide. Increasing the pH to 10-11 was found to have an accelerating effect, as well as increasing the temperature and nickel catalyst concentration. A similar disclosure is to be found in US Patent No. 3.023.223.
[0011] In EP 1 647 540. L-iditol is prepared starting from sorbitol. In a first step sorbitol is converted by fermentation into L-sorbose, which is subsequently hydrogenated into a mixture of D-sorbitol and L-iditol. This mixture is then converted into a mixture of L-iditol and L-sorbose. After separation from the L-sorbose, the L-iditol can be converted into isoidide. Thus, sorbitol is converted into isoidide in a four-step reaction, in a yield of about 50%.
[0012] A preferred method for preparing isoidide by the epimerization of isosorbide is described in European Patent Application No. 12156170.8, filed Feb. 20, 2012 for "Method of Making Isoidide". wherein a supported ruthenium catalyst is used at a starting pH of above 7, preferably of from 8 to 10, with the starting pH referring to the pH of the aqueous solution of isosorbide.
[0013] The epimerization of isosorbide into isoidide is conducted according to this process under relatively mild conditions, such that an equilibrium production of isoidide can be attained while avoiding mass losses through hydrodeoxygenation and providing a better overall yield compared to the results of Wright and Brandner.
[0014]The support can vary widely, including silica, alumina, titania, zirconia, and carbon. A carbon support is preferred, inter alia since it can be operated at a wider pH range than other supports. As well, a carbon
supported ruthenium catalyst was observed to act more favorably in the epimerization of isosorbide, than other supports, e.g., AI203. The catalytically active metal preferably consists essentially of ruthenium, and the support preferably consists essentially of carbon. A suitable ruthenium content is described as from 1% to 10% by weight of ruthenium, based on the total weight of the catalyst, preferably being about 5% by weight of the catalyst. [0015] In order to conduct the epimerization, isosorbide is provided in the form of an aqueous sofution. The concentration of isosorbide therein may widely vary. However, for the sake of process economics as well as results in terms of yield, it is preferred for the isosorbide concentration to be in a range of from 25% by weight to 75% by weight. More preferably, the isosorbide concentration is 30% to 60% by weight- The optimum concentration is believed to approximately 50% by weight.
[0016] The aqueous solution is subjected to an atmosphere comprising hydrogen. The hydrogen pressure can widely vary, for example, from 20 to 200 bars. However, it was found particularly effective to employ a relatively low pressure in the range of from to 55 bars, and preferably about 40 bars.
[0017] Calculated on the basis of a water paste comprising 50% of a 5% ruthenium on carbon catalyst, the catalyst concentration in the reactor, calculated as a weight percentage based on the aqueous solution of isosorbide, can range from as low as, e.g., 1% to as high as, e.g. 50%.
However, for the sake of process economics as well as results in terms of yield and specificity, it is preferred for a 5% ruthenium catalyst to be employed in a concentration of from 2 to 20%, and more preferably about 4%. it will be understood that these percentages will hold, mutatis mutandis, for other water paste concentrations than 50%, and other catalyst loadings than 5%.
[0018] The skilled person will be aware of how to generally conduct the ruthenium catalyzed reaction. Background references in this respect include US 6,177,598 and US 6.570,043.
[0019] The ruthenium catalyst as mentioned preferably comprises a carbon support. Different types of carbon support are contemplated and may be used. e.g. activated carbon or carbon nanotubes. The activated carbon can be, e.g., 50-70% wetted powder. Typically preferred catalysts include commercial ruthenium on carbon catalysts ex BASF or Evonik (Strem
Chemicals). A background reference on Ru/C catalysts is Sifontes Herrera et al, J. Chem Technol Biotechnol (2011), "Sugar hydrogenation over a Ru/C catalyst."
[0020] The epimerization reaction is conducted preferably at an elevated temperature, i.e. above 20°C, and preferably below 250°. A preferred temperature range is 200° to 240°, most preferably about 220°C. The duration of the reaction will generally be shorter at higher temperatures. The residence time in the reactor where the isosorbide solution is subjected to hydrogen under the influence of the catalyst, will generally range from 0.1 to 10 hours, preferably. 0.25 to 4 hours, and more preferably 1-2 hours.
[0021] It is preferred to adjust the pH of the aqueous solution of isosorbide. Although, for the sake of conducting the epimerization per se, the pH may widely vary, it has been found that unwanted side reactions, which lead to loss of matter as a result of the formation of volatiles, can be reduced considerably by adjusting the pH to a value of 8 to 10.
[0022] From the equilibrium mixture, the isoidide starting material can be recovered by separation methods known to the skilled person, such as by chromatographic techniques, selective crystallization or distillation. The latter can be conducted, e.g. as disclosed by Wright et al., J. Org. Chem., 1964, 29 (10), pp 2979-2982, mentioned above.
[0023] In like manner, isosorbide-3,6~dicarboxylic acid was also successfully prepared from isosorbide, according to the procedure described in Example 2 below. The isosorbide starting material can be obtained by any known method for making isosorbide, for example, as described in US
7,420,067 to Sanborn or as described in US 6,849,748 or 7,439,352, both to Sanborn et al.
[0024] The present invention is further illustrated by the examples which follow:
[0025] Example 1
[0026] For preparing the isomannide 3,6-dicarboxylic acid, initially (3S,3aS,6S,6aS)-hexahydrofuroI3,2-b]furan-3.6-diyl
bis(trifluoromethanesulfonate) was prepared:
Figure imgf000008_0001
[0027] in a procedure adapted from ChemSusChern 2011, 4, pp. 599- 603, a 50 mL oven dried boiling flask was charged with 2 g of isoidide, 85 mg of 4-dimethylaminopyridine, 2.44 mL of dry pyridine, and 25 mL of dry dichloromethane. The homogeneous solution was chilled to about 0 deg. C in a brine/ice bath, and while vigorously stirring under a N2 blanket, 4.5 mL of trifluoromethanesulfonic anhydride was added dropwise via syringe. After complete addition, a gelatinous, stationary mass was observed, which dissolved upon attaining room temperature. The reaction proceeded overnight at room temperature, after which the solution was poured over a Celite pad, the filtrate washed with 100 mL of 1M HCl. and the methylene chloride phase dried over anhydrous magnesium sulfate, furnishing 5.22 g of a loose, white precipitate after concentration in vacuo (93%). Elemental Analysis: Predicted for C8H8F608S2 409.9565: Found 409.9559.
[0028] From the isomannide ditriflate prepared as described, the dinitrile (lUPAC (3R,3aR,6R,6aR)-hexahydrofurol3,2-b]furan-3,6- dicarbonitrile) was then prepared.
[0029] In doing so, an oven-dried 250 mL round bottomed flask was charged with 1.54 g of potassium cyanide (23.6 mmol), 6.24 g of 18~crown~6 (23.6 mmol) and 75 mL of anhydrous THF; the mixture was chilled to about 0 deg. C in a saline/ice bath and purged with argon. A separate, oven-dried 100 mL round bottomed flask was charged with 4.4 g of 3S,3aS,6S,6aS- hexahydrofuro[3,2-b}furan-3.6-diyl bis(trifluoromethanesulfonate (isoidide ditriflate) and 25 mL of anhydrous THF. This mixture was then added dropwise to the cyanide/18-crown-6 solution (over a period of about 10 min). After addition, the heterogeneous solution was allowed to warm to room temperature and stirred for 5 hours.
[0030] After this allotted time, the slightly darkened solution was poured over 50 mL of ice water, 50 ml of methylene chloride was added, and the resultant Diphasic solution was transferred to a 250 mL separatory funnel. Here, the bottom organic phase was removed, washed twice with 50 mL of water, and concentrated in vacuo to produce 8.10 g of a dark, seemingly insoluble precipitate. Approximately 2 g of this material was triturated with 100 mL of dichloromethane for 1 hour, the solids were filtered off, and the solution concentrated in vacuo, producing about 1.600 g of a crude, light- yellow semisolid. This material was then dissolved in a minimum amount of methylene chloride, adsorbed to about 20 g of silica gel (60A, 40-63 μΜ, 230 x 400 mesh), dried under vacuum, and added to a prefabricated silica gel column.
[0031] Flash chromatography ensued using a gradient 1 :1 to 1 :3
Hexane (Hex)/Ethyl Acetate (EtOAc) mobile phase proportion, monitoring the elution of products by GC/MS (CI) and TLC (cerium molybdate stain). The initial products (diastereomers) eluted as 20 cc fractions at 1 :1 Hex/EtOAc with a rf of -0.6 (1:1 Hex/EtOAc). After concentration, 130 mg of a clear semi-solid was obtained. High resolution (HR) GC/MS revealed signals at 14.00 min and 15.28 min and manifested the same mass spectra
fragmentation pattern for each with a molecular ion of 138.0573 m/z. 1 H NMR of diastereomer A; (400 MHz, CDCI3), δ 5.30 (d. J = 4.6 Hz, 1H), 4.99 (t, J = 4.2 Hz, 1H), 4.76 (d, J = 5.0 Hz, 1H), 4.18-4.16 (m. 2H), 4.10-4.09 (m, 1H), 3.25 (m, 1H). 1H NMR of diastereomer B (400 MHz, CDCI3), δ 5.28 (d, J = 4.6 Hz, 1H), 5.08 (t, J = 4.2 Hz, 1H), 4.84 (d. J = 5.0 Hz, 1 H), 4.16-4.14 (m, 2H). 4.06-4,04 (m, 1H), 3.91 (t, J = 4.2 Hz. 1H). The spectral data is consistent with the following structures (3R,3aR,6aR)-2,3,3a,6a- tetrahydrofuro[3,2-b]furan-3-carbonitrile and (R) or (S)-2,3,5.6- tetrahydrofuro[3,2-b]furan-3-carbonitrile:
Figure imgf000010_0001
[0032] Further structural elucidation as well as absolute stereochemical assignments will follow for the proposed compounds is in progress.
[0033] The penultimate molecular entity to elute did so in 20 cc fractions 33-46 at 1 :2 Hexane/EtOAc composition, with a rf of 0.1 (1:1
Hex/EtOAc) and 0.3 (1:2 Hex/EtOAc). Inspissations under vacuum afforded approximately 100 mg of a white semi-solid. HR GC/MS disclosed a single peak at 15.72 min with a molecular ion of 165.0674 m/z. 1H NMR (400 MHz, CDCI3), δ 5.00-4.96 (dd. J = 5.6, J = 2.2 Hz. 1H), 4.88 (t, J - 4.2 Hz, 1 H), 4.23 (t, J = 5.0 Hz, 1H), 4.14-4.10 (m, 2H), 4.07 (t, J - 5.8 Hz, 1H), 3.22-3.20 (m, 2H). The spectral data is consistent with the following structures
(3R,3aR,6S,6aR)-hexahydrofuro[3,2-b]furan-3,6-dicarbonitrile - enantiomer):
Figure imgf000010_0002
[0034] The last molecular entity to elute occurred in 20 cc fractions 62- 67 at a eluent ratio of 1 :3 Hexane/EtOAc, and manifested an rf of 0.1 (1:2 Hex/EtOAc). Concentration of this material under vacuum afforded
approximately 120 mg of a translucent semi-solid. HR GC/MS conveyed a single peak at 17.04 min with a molecular ion of 165.0509. The
fragmentation pattern was congruent with the aforementioned dinitrile. This was confirmed with GC/MS (EI) which revealed a peak at 35.638 min and a salient fragment at 137.0. 1H NMR (400 MHz, CDCI3). δ 4.88 (d, J = 4.4, 2H), 4.29 (t, J = 4.0 Hz, 2H). 4.11 (t, J = 4.2 Hz, 2H), 3.27 (m, 2H); 13C NMR (100 MHz, CDCI3) δ 115.13, 83.11 , 70.87, 36.66. The spectral data is consistent with (3R,3aR,6R,6aR)-hexahydrofuroI3,2-bIfuran-3,6-dicarbonitrile.
Figure imgf000011_0002
[0035] Approximately 6 grams of black precipitate remains crude. The total crude recovered was about 8 grams, so it can be assumed that similar yields of the aforementioned molecular entities would be observed upon serial flash chromatographic sequestration. Hence, the overall quantities of
(3R,3aR,6S,6aR)-hexahydrofuro[3,2-b]furan-3,6-dicarbonitrile and enantiomer is calculated to be about 400 mg (23%) and that of the 3R,3aR,6R,6aR)- hexahydrofuro[3,2-b]furan-3,6-dicarbonitrile to be about 480 mg (27%).
Collectively, the actual yield of isomannide dinitrile is 50%.
[0036] Following preparation of the dintrile, the isomannide 3.6- dicarboxylic ((35, 3aS, 6S, 6aS)-hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid) was prepared from the dinitrile:
Figure imgf000011_0001
[0037] A 10 mL round bottomed flask was charged with 100 mg of the (3S,3aS,6S,6aS)-hexahydrofuro[3,2-b]furan-3,6-dicarbonitrile 1 (0.6 mmol) and 3 mL of concentrated hydrochloric acid (~ 12 M). The resulting
suspension was then stirred at 75 deg. C under argon for 6 hours. After this time, the light yellow solution was cooled to room temperature, then with a short path condenser under reduced pressure (10 torr) and with gentle heating (50 deg. C) was concentrated. A beige colored precipitate was observed after 2 hours, weighing 115 mg, and was determined to be
(3S,3aS,6S,6aS)-hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid 2 (95%) by spectroscopic analysis. 1H NMR (d6~DMSO, 400 MHz) δ (ppm) 12.45 (s. 2H), 4.75 (d, J = 6.2 Hz, 2H), 3.83 (t, J = 4.2 Hz, 2H), 3.79 (t, J = 4.4 Hz. 2H). 3.23-3.21 (m, 2H); 13C NMR (d6-DMSO. 100 MHz) δ (ppm) 170.10. 83.92, 68.98, 50.49.
[0038] Example 2
[0039] The isosorbide-3,6-dicarboxylic acid (IUPAC (3R,3aR,6S.6aR)- hexahydrofuro[3.2-b]furan-3,6-dicarboxylic acid) was synthesized, corresponding to structure 4 in the formula, in a series of steps:
Figure imgf000012_0001
[0040] Initially, isosorbide-3.6-ditriflate (lUPAC (3R,3aS,6S,6aS)- hexahydrofuro[3.2-b]furan-3,6-diyl-bis(trifluoromethanesulfonate),
corresponding to structure 2) was prepared from isosorbide (structure 1).
Figure imgf000012_0002
[0041] A 100 ml, two neck boiling flask containing a magnetic stir bar was charged with 1.00 g of isosorbide (6.84 mmol), 4.25 g of triflic anhydride (15.05 mmol), and 30 mL of anhydrous THF. An argon inlet adapter and rubber septum were then fitted to the flask ports, and the mixture was chilled to about 0 deg. C in an ice/brine bath. While stirring and under an argon blanket, 1.65 mL of pyridine (20.5 mmol) was injected dropwise via a syringe over a 5 minute period. Once added, the brine bath was removed and the reaction continued at room temperature for 2 hours, by which time TLC (4:1 EtOAc/MeOH) indicated that all isosorbide had been consumed. Excess solvent and pyridine was evaporated under vacuum and the syrupy residue dissolved in about 2 mL CH2CI2 before being directly charged to a prefabricated silica gel flash column (Hex/EtOAc). The target,
(3R,3aS,6S,6aS)-hexahydrofuro[3.2-b]furan-3,6-diyl bis(trifluoromethanesulfonate) 2, was observed to elute with a 4:1 Hex/EtOAc mobile phase (cerium molybdate stain), rf 0.7 (1 :1 Hex/EtOAc) producing 2.25 g of a white precipitate after drying (81%). 1H NMR (d6-DMSO, 400 MHz) δ 5.52 (m, 2H), 4.26 (m, 2H), 3.99 (m, 2H), 3.55 (m, 2H); Elemental Analysis: Predicted C (23.42%) H (1.97%); Found C (23.48%) H (1.99%).
[0042] The isosorbide 3,6-dinitrile (lUPAC (3R,3aR,6S,6aR)- hexahydrofuro[3.2-b]furan-3,6-dicarbonitrile, corresponding to structure 3) was then prepared.
Figure imgf000013_0001
[0043] An oven dried. 100 mL boiling flask was charged with 349 mg of potassium cyanide (5.36 mmol), 1.42 g of 18 crown 6 (5.36 mmol), and 10 mL of anhydrous THF. The heterogeneous mixture was then chilled to 0 deg. C in an ice/brine bath. In a separate 50 mL boiling flask, 1.00 g of the
isosorbide ditriflate (2.44 mmol) was dissolved in 10 mL of THF, then the solution was poured into a 50 mL addition funnel and added to the cyanide solution at a rate of -2 mL/min. Once the entire volume had been added, the mixture was removed from the ice/brine bath and the reaction continued at room temperature for another 2 hours. At this time, a deep red solution was observed, and multiple spots developed on a silica gel TLC plate. The solvent was evaporated under vacuum, the remainder dissolved in a minimum amount of CH2CI2 and charged to a prefabricated silica gel column. Carefully monitored flash chromatography was then conducted with gradient CH2CI2 to EtOAc eluents. Three distinct fraction sets were collected; those
corresponding to isosorbide dinitrile transpired with an eluent ratio of 6 1 EtOAc/CH2CI2, and after drying, produced 333 mg of a deep-yellow semisolid (81%). 1H NMR (d6-DMSO, 400 MHz) δ 5.26 (m, 2H), 4.09 (m. 2H), 4.02 (m, 2H), 3.37 (m, 2H); HRMS (M+H) Predicted for C8H9N202:
165.0664; Found 165.0662. [0044] Following preparation of the isosorbide dinitrile as described, the isosorbide 3,6-diacid was made (lUPAC (3R,3aR,6S,6aR)- hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid, corresponding to structure 4).
Figure imgf000014_0001
[0046] A 10 mL round bottomed flask was charged with 100 mg of the isosorbide-3,6-dinitrile (0,6 mmol) and 3 mL of concentrated hydrochloric acid (about 12 M). The resulting suspension was then stirred at 75 deg.C under argon for 6 hours. After this time, the reddish solution was cooled to room temperature, then concentrated with a short path condenser under reduced pressure (about 10 torr) and with gentle heating (50oC). A dark brown precipitate was observed after overnight drying, weighing 111 mg (90%), and this was determined to be isosorbide-3,6-dicarboxylic acid spectroscopically. 1H NMR (D20, 400 MHz) δ 4.89 (m. 2H), 4.01 (m, 2H), 3.89 (m, 2H), 3.22 (m, 2H); HRMS (M+) Predicted for C8H10O6: 202.0477; Found. 202.0466.

Claims

1. (3S, 3aS, 6S, 6aS)-hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid.
2. (3R, 3aR, 6S, 6aR)-hexahydrofuro[3,2-b]furan-3,6-dicarboxylic acid.
3. The dicarboxylic acid of isomannide.
4. The dicarboxylic acid of isosorbide.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116554193A (en) * 2023-05-22 2023-08-08 吉林大学 Isosorbide derived dibasic ester, acid and alcohol monomer and synthesis method thereof
KR102638391B1 (en) * 2023-05-30 2024-02-20 삼화페인트공업주식회사 Method for producing dialkanesulfonyl isosorbide compound, electrolyte additive for lithium secondary battery, electrolyte for lithium secondary battery, and lithium secondary battery

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090301348A1 (en) * 2007-02-05 2009-12-10 Evonik Oxeno Gmbh Mixture of diesters of dianhydrohexitol derivatives with carboxylic acids of the empirical formula c8h17cooh, process for preparing these diesters, and use of these mixtures
US20100160548A1 (en) * 2006-09-15 2010-06-24 Bart Adrianus Johannes Noordover Process for the production of a dianhydrohexitol based polyester
WO2011144353A1 (en) * 2010-05-20 2011-11-24 Stichting Dutch Polymer Institute New biobased chiral compounds

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100160548A1 (en) * 2006-09-15 2010-06-24 Bart Adrianus Johannes Noordover Process for the production of a dianhydrohexitol based polyester
US20090301348A1 (en) * 2007-02-05 2009-12-10 Evonik Oxeno Gmbh Mixture of diesters of dianhydrohexitol derivatives with carboxylic acids of the empirical formula c8h17cooh, process for preparing these diesters, and use of these mixtures
WO2011144353A1 (en) * 2010-05-20 2011-11-24 Stichting Dutch Polymer Institute New biobased chiral compounds

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
JING WU ET AL.: "Isohexide derivatives from renewable resources as chiral building blocks", CHEMSUSCHEM, vol. 4, 2011, pages 599 - 603 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116554193A (en) * 2023-05-22 2023-08-08 吉林大学 Isosorbide derived dibasic ester, acid and alcohol monomer and synthesis method thereof
KR102638391B1 (en) * 2023-05-30 2024-02-20 삼화페인트공업주식회사 Method for producing dialkanesulfonyl isosorbide compound, electrolyte additive for lithium secondary battery, electrolyte for lithium secondary battery, and lithium secondary battery

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