Oxidation of 5-hydroxy-2-furanone to maleic acid ester

Abstract

The present invention relates to a method for preparing maleic acid or a derivative thereof, comprising step b) oxidizing 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid to maleic acid or a derivative thereof by contacting the 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid with molecular oxygen (O) in the presence of a catalyst. In certain embodiments, step b) is preceded by step a) of oxidizing a furan compound of formula I to 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid, TIFF2022514771000009.tif48146 Here R 1 is H, CH2OH, CO2H or CHO, and R 2 is H, OH, C1-C6 alkyl, or O(C1-C6 alkyl), or esters, ethers, amides, acid halides, anhydrides, carboximidates, nitriles, and salts thereof.

Description

[Technical field]

[0001] The present invention relates to the field of chemical preparation of maleic acid and its derivatives. In particular, the present invention relates to the sustainable chemical preparation of maleic acid and its derivatives using biomass-derived starting materials. [Background technology]

[0002] Current industrial maleic acid production methods are generally based on the hydrolysis of maleic anhydride, which itself is produced by oxidation of petrochemicals such as butane or benzene. In order to reduce the environmental footprint of the production and provide a more sustainable route for maleic acid production, it is desirable to replace petrochemicals with biomass-derived chemicals, see for example, Non-Patent Document 1.

[0003] For example, Non-Patent Document 2 describes the chemical oxidation of furfural, a biomass-derived chemical, with hydrogen peroxide. The use of hydrogen peroxide for the oxidation of furfural to produce maleic acid is also reported in Non-Patent Document 3. The drawback of such chemical oxidation reactions is that they require hydrogen peroxide as an oxidizing agent, which must be prepared by a separate production method, is relatively expensive, and is consumed in the reaction, thus reducing the overall advantage of using biomass-derived chemicals.

[0004] Alternatively, furfural can be electrochemically oxidized as described in US Pat. No. 5,399,414, US Pat. No. 5,363,666, and US Pat. No. 5,399,671. However, the drawbacks of both of these known methods for preparing maleic acid are that furfural is used as a starting material, and the one-pot oxidation method is time-consuming and generally requires a mediator to achieve an acceptable reaction rate. However, the mediator is expensive and difficult to recycle, so it is generally not preferred for large-scale production. [Prior art documents] [Patent documents]

[0005] [Patent Document 1] UK Patent Application Publication No. 253877 [Patent Document 2] China Patent Publication No. 108314647 [Non-patent literature]

[0006] [Non-Patent Document 1] Wojcieszak et al. (Sustainable Chemical Processes, 2015, 3:9, 1-11) [Non-Patent Document 2] Journal of Organic Chemistry, 1986, 51(4), 567-569; [Non-Patent Document 3] Badovskaya et al. (Russian Journal of General Chemistry, 2018, 88(8), 1568-1579) [Non-Patent Document 4] Mil'man et al. (Elektrokhimiya, 1978, Volume: 14, Issue: 10, 1555-1558) [Non-Patent Document 5] Hellstrom et al. (Svensk Kemisk Tidskrift, 1948, Volume 60, 214-220) [Non-Patent Document 6] Galles et al. (J. Am Chem. Soc. 2013, 135, 19143-19146) [Non-Patent Document 7] Synthesis 2012,44(16),2560-2566 [Non-Patent Document 8] Catalysis Communications 2010, 11(13), 1081-1084 [Non-Patent Document 9] Tetrahedron Letters 2010, 51(26), 3360-3363 [Non-Patent Document 10] Synthesis 2009, (11), 1791-1796 [Non-Patent Document 11] Chemistry Letters 2004, 33(9), 1142-1143; 2004 [Non-Patent Document 12] Bull. Chem. Soc. Japan 2006, 79(12), 1983-1987 Summary of the Invention [Problem to be solved by the invention]

[0007] It would be desirable to provide a method for preparing maleic acid with high atom efficiency from biomass, particularly from biomass-derived furan compounds. [Means for solving the problem]

[0008] The present inventors have discovered that in certain oxidation processes, such as electrochemical processes of furan compounds, the tautomers 5-hydroxy-2(5H)-furanone (also referred to herein as HFO) and cis-β-formylacrylic acid (also referred to herein as formylacrylic acid) are produced as intermediates. [ka]

[0009] Without wishing to be bound by theory, it is believed that the closed ring form (i.e., 5-hydroxy-2(5H)-furanone) cannot be electrochemically oxidized, or can be oxidized only very slowly, which prevents this oxidation. In many environments and conditions, the chemical equilibrium is almost entirely in favor of the furanone, which can lead to a slow reaction, especially in atom-efficient electrochemical oxidation methods. This slow reaction could be overcome by a chemical oxidation reaction using hydrogen peroxide, but the use of hydrogen peroxide is not preferred, among other reasons mentioned above.

[0010] However, the present inventors have surprisingly discovered that 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid can be oxidized to maleic acid or its derivatives by molecular oxygen (O2), also called oxygen.

[0011] The present invention is therefore directed to a process for the preparation of maleic acid or a derivative thereof, comprising the step of oxidizing 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid to maleic acid or a derivative thereof by contacting with molecular oxygen (O2) in the presence of a catalyst, which step is referred to herein as step b).

[0012] The inventors have found that several metals, particularly transition metals, are suitable for catalysing the oxidation reaction of step b), with particularly good results being obtained with copper, gold, palladium, platinum and ruthenium, especially gold.

[0013] The catalyst preferably further comprises a solid support. The solid support may be any support known in the art and may be any common support as long as it does not adversely affect the oxidation reaction. In general, the solid support is inert in step b). Examples of supports found to be suitable for the present invention include activated carbon, aluminum oxide, zinc oxide, and titanium dioxide. Titanium dioxide as a solid support has been shown to give particularly good results in terms of maleic acid yield, especially in combination with gold.

[0014] Step b) of the present invention is generally carried out in the liquid phase, not in the gas phase. Furan compounds and HFOs are unstable at the high temperatures required to keep them in gaseous form, so reaction conditions in the gas phase are not well suited for the present invention. Therefore, it is preferred that the HFO and / or formylacrylic acid are liquid or dissolved in a solvent when contacted with O2. Preferred solvents include both organic and aqueous solvents. Water-immiscible organic solvents and acidic aqueous solvents are particularly preferred for reasons detailed below. Good conversion of HFO and / or formylacrylic acid was obtained in water, aqueous sulfuric acid, acetic acid, ethyl acetate, methyl isobutyl ketone (MIBK), methyl tert-butyl ether (MTBE), 2-methyltetrahydrofuran (2-MeTHF), dichloromethane, heptane, acetonitrile, acetone, nitromethane and toluene, preferably 2-MeTHF, toluene and MTBE.

[0015] The solvent in which step b) is carried out can affect the products formed. For example, in organic solvents, maleic anhydride can be produced by in situ dehydration of maleic acid or when HFOs are directly oxidized by a catalyst. On the other hand, in aqueous solvents, usually under acidic conditions, maleic acid itself is generally produced, and under basic conditions, maleate salts can be produced. Also, under certain reaction conditions, maleic acid can be at least partially isomerized to fumaric acid. The reaction conditions in which step b) is carried out generally also affect the products formed.

[0016] It has been found that the oxidation process gives the best results in terms of conversion under mild reaction conditions, including only slight increases in temperature and pressure. Step b) is therefore preferably carried out under a pressure of at least 5 bar, preferably at least 10 bar. The preferred temperature range for carrying out step b) is from 20 to 200° C., more preferably from 50 to 150° C., most preferably from 60 to 100° C. These conditions allow the reaction to be carried out continuously, preferably in a tubular reactor or the like. The reactor may optionally contain a fixed catalyst bed containing the catalyst. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0017] The starting HFO and / or formylacrylic acid may be supplied or provided to step b) as an isolated (i.e. substantially pure) preparation or as a reaction mixture derived from a prior process. The isolated preparation may be obtained by a prior process and isolation that is not part of the present invention. This prior reaction may be any type of reaction process, for example where HFO and / or formylacrylic acid are produced as main products or where HFO and / or formylacrylic acid are produced therein as by-products. In a preferred embodiment of the present invention, the HFO and / or formylacrylic acid are derived from one or more furan compounds derived from biomass.

[0018] (Details of step a) In a preferred embodiment shown in Scheme 2, step b) is preceded by step a) of oxidizing the furan compound of formula I to 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid, where R 1 is H, CH2OH, CO2H or CHO, R 2 is H, OH, C1-C6 alkyl or O(C1-C6 alkyl), or esters, ethers, amides, acid halides, anhydrides, carboximidates, nitriles, and salts thereof. [ka]

[0019] The electrochemical oxidation of furan compounds of formula I is described in detail in PCT / NL2018 / 050881, which is incorporated herein in its entirety. It has been found that the combination of step b) with the electrochemical oxidation of furan compounds according to the present invention is particularly beneficial, since it has been found that the equilibrium between HFO and formylacrylic acid at the preferred pH of the electrochemical oxidation is almost entirely on the side of HFO, resulting in a slow oxidation. The reaction rate of the electrochemical oxidation can be made acceptable by using a mediator, but the presence of a mediator is not preferred, especially on a large scale. Common mediators are expensive, and large-scale processes would require recycling or immobilization of the mediator to make the process economically viable. Step b) of the present invention shows a good reaction of HFO and formylacrylic acid, so the two-step process including steps a) and b) is generally preferred.

[0020] In a preferred embodiment, the furan compound comprises a 2-furoic acid compound or an ester thereof, which is advantageously more stable than furfural and can be obtained as a by-product in the production of 2,5-furandicarboxylic acid (FDCA) or by stabilization of furfural by direct oxidation of furfural to furoic acid, a process generally carried out under mild conditions (e.g., reaction temperature below 100°C). Therefore, the use of 2-furoic acid compounds is preferred. Furthermore, since it is believed that there is currently no large market for furoic acid, it is also beneficial to use furoic acid in the chemical process of the present invention.

[0021] The use of furoic acid to produce maleic acid, substituting furfural with furoic acid, has been found to be particularly advantageous in electrochemical oxidation reactions. Electrochemical reactions tend to have significantly longer residence times than thermochemical reactions (due to limited surface area of ​​the electrodes and mass transfer to / from the surface, see below), so that chemicals often spend much longer in solution where they are susceptible to degradation. Therefore, electrochemical oxidation methods for preparing maleic acid particularly benefit from increased stability of the starting materials. Thus, the oxidation comprises electrochemical oxidation in an electrolyte solution, typically in an aqueous electrolyte solution containing such furoic acid compounds. Or, in the first embodiment, preferably, the oxidation consists of electrochemical oxidation in an electrolyte solution, typically in an aqueous electrolyte solution containing such furoic acid compounds. Therefore, the addition of an oxidizing agent such as hydrogen peroxide may not be required. Generally, such methods comprise dissolving a furoic acid compound in an electrolyte solution, followed by electrochemical oxidation to convert such furoic acid or its derivatives to maleic acid.

[0022] In yet another preferred embodiment, the furan compound comprises furfural. Advantageously, the in situ electro-oxidation to 2-furoic acid is simple, rapid, and can be carried out at ambient temperature, limiting the decomposition of furfural. Furfural also has a high solubility in water (about 83 g / L). Furthermore, starting with furfural reduces the overall reaction step by one. Starting with furfural is particularly preferred for scaling up the method of the present invention.

[0023] A particular embodiment of the present invention includes chemically catalytic oxidation of furfural to furoic acid prior to electrochemical oxidation of furoic acid. By furoic acid compound is meant any compound based on 2-furoic acid and having the same oxidation state as furoic acid, such that it can be oxidized to maleic acid. Examples of preferred furoic acid compounds include 2-furoic acid, furoic acid esters, furoic acid amides, furonitrile, furoic acid anhydride, furoic acid carboxyimidates, furoic acid halides, furoic acid salts, etc. In particular, 2-furoic acid is preferably used as the furoic acid compound due to its high solubility in water (about 37.1 g / L in water at 15° C. and about 100 g / L in water at 50° C.).

[0024] The electrochemical oxidation according to step a) of the present invention is preferably carried out using one or more working electrodes (herein referred to as anodic electrodes, anodes or simply electrodes) comprising lead oxide, e.g. PbO2, optionally supported on a metal such as Pb, activated carbon, carbon nanotubes (CNTs), reticulated vitreous carbon (RVC), porous graphite such as carbon felt, or titanium support, or boron doped diamond (BDD). The activity of the electrodes can be improved by adding dopants or adatoms (to the electrode or electrolyte). For example, Fe 2+ or Fe 3+ The stability of PbO2 can be improved by adding metal ions such as ZnO, Fe, and Cu to the electrolyte. In principle, any electrode structure, such as two-dimensional or three-dimensional structures, may be used, but one or more electrodes including one or more porous electrodes, fused electrodes, mesh electrodes, nanostructured electrodes, metal or metal oxide particles supported on porous carbon / graphite electrodes, or combinations thereof, are preferred. Such electrodes provide higher conversion efficiency. In certain embodiments, the working electrode may alternatively or additionally include one or more of mixed metal oxides (MMO), dimensionally stable anodes (DSA), stainless steel, brass-carbon based graphite electrodes, boron-doped diamond (BDD), Mn (e.g., MnO2), Pt, Au, Ag, Cu, Ir, Ru, Pd, Ni, Co, Zn, Cd, In, Sn, Ti, Fe, and alloys or oxides thereof.

[0025] The counter electrode (referred to as the cathodic electrode or cathode) may comprise one or more materials selected from the group consisting of Au, Pt, Pd, Ir, Ru, Ni, Co, stainless steel, Cu, carbon, Pb, Ti or alloys thereof.

[0026] In one embodiment, the working electrode is doped with a mediator. The inventors have surprisingly found that vanadium-doped electrodes are particularly suitable for carrying out the method. Thus, vanadium-doped electrodes are another aspect of the present invention. In this embodiment, the pH of the electrolyte solution is preferably in the range of 3 to 7, more preferably 4 to 5, to limit the dissolution of vanadium. Also suitable is a combination of V2O5 and PbO2, with V2O5 being kept dissolved in the electrolyte. For recycling purposes, the catalyst V2O5 is preferably attached to a support. Furthermore, PbO2, cations (Fe 3+ , Co 2+ , and Ni 2+ Doping of PbO2 with cations such as cations, F-, or both cations and F- can be a means to improve the stability and electrochemical activity of the electrode in processes conducted at high potentials.

[0027] The oxidation of furan compounds can occur directly at the electrode. This means that electrons from the oxidant or electrode are transferred directly to the furan compound or chemical intermediate in the reaction. Alternatively, oxidation can occur by using a mediator that is reduced or oxidized at the electrode surface and then reacts with the target compound at the bulk of the electrode. Although the presence of a mediator does not preclude the possibility of oxidation at the electrode, generally, when a mediator is present, oxidation proceeds primarily through the mediator. Mediators can be one or more of vanadates, vanadium oxides (e.g., V2O5, VO2), molybdates (MoO4 2- ), chromate (CrO4 2- ), dichromate (Cr2O7 2- ), permanganate (MnO4 - ) Manganate (MnO42- ), manganese salts (Mn 2+ ), tungstate (WO4 2- ), iodate (IO3 - ), chlorate (ClO - ), chloride-chlorine pair (Cl - / Cl2), bromate (BrO - ), bromide-bromine vs. Br - / Br2, peroxydisulfate (S2O8 2- ), ozone (O3), cobalt salts (Co 2+ / Co 3+ ), cerium salts (Ce 3+ / Ce 4+ ) and the like. Most preferably, the mediator comprises vanadium oxide, sodium molybdate, and / or potassium dichromate.

[0028] The mediator may be immobilized, for example in close proximity or at the working electrode, but a drawback of immobilization is likely to be leaching of the mediator and that immobilization limits the amount of mediator available (due to the limited surface area of ​​any support), which may also limit the rate of large-scale production.

[0029] Surprisingly, the inventors have found that the oxidation reaction proceeds satisfactorily without any mediator. Due to costs, safety issues (mediators are often highly toxic / carcinogenic), increased process complexity (mediator recovery / recycling), and the environmental footprint of the process, it may be preferable to carry out the process without such mediators. Therefore, it is preferable that the electrolyte solution is substantially free of such mediators during the electrochemical oxidation. In the context of the present invention, substantially free means preferably less than 5 mol%, preferably less than 1 mol%, more preferably less than 0.01 mol%, based on the amount of furan compound starting material present at the start of the electrochemical oxidation reaction. Most preferably, the electrolyte solution contains no more than trace amounts of mediators. Note that "at the start of the electrochemical oxidation reaction" means just before the first amount of furan compound is oxidized.

[0030] The oxidation, especially the electrochemical oxidation, of step a) proceeds particularly well in a certain pH range. The particularly preferred pH range depends, inter alia, on the electrode and the oxidizing agent used, but is generally close to the pK a The pH value may in part determine the preferred pH range, particularly when the furan compound comprises 2-furoic acid, and the electrochemical oxidation is preferably, at least in part, carried out at a pH of less than 7, more preferably less than 4, even more preferably less than 3, and most preferably about 2 or less.

[0031] The conversion of the furan compound to formylacrylic acid may cause the pH of the electrolyte solution to fall below the value at the start of the reaction. It may therefore be possible to start the electrochemical oxidation at a pH value above the optimum value for carrying out the oxidation and to allow the pH value to fall during the conversion of the furan compound to the optimum pH value or to the preferred pH value as defined above. The preferred pH value is therefore defined for at least part of the reaction period of the electrochemical oxidation (see above: "at least partly carried out at a pH of . . . ") and not necessarily for the entire reaction period of the electrochemical oxidation. However, in some embodiments, concentrated sulfuric acid is used as the electrolyte and the change in pH may generally be very small.

[0032] The pH can be adjusted externally during the reaction (e.g., by addition of a suitable acid or base) to maintain an optimal pH over the entire reaction period. Additionally, the reaction can be carried out in the presence of a buffer to maintain the pH. Additionally, the desired pH range can be achieved by using a suitable solvent or a suitable electrolyte solution. Thus, when a solvent or electrolyte solution is present, it is preferred to include an acid such as an organic acid and / or a mineral acid. Mineral acids are preferred because they are more inert in electrochemical oxidation reactions compared to organic acids. More preferably, the mineral acid is selected from the group consisting of hydrochloric acid (HCl), nitric acid (HNO3), phosphoric acid (H3PO4), sulfuric acid (H2SO4), boric acid (H3BO3), hydrofluoric acid (HF), hydrobromic acid (HBr), perchloric acid (HClO4), and hydroiodic acid (HI). Most preferably, the electrolyte solution includes sulfuric acid, since persulfates can be formed at the PbO2 electrode when an oxidizing potential is applied to the PbO2 electrode. Persulfates are also strong oxidizing agents. In certain embodiments, the acid may be at least partially immobilized by incorporation into a resin (such as Amberlyst® or Nafion®) that may be added to the mixture, and / or the acid may be structurally incorporated into one or more electrodes. In certain embodiments, it may be preferred that the electrolyte includes an acid in combination with an inorganic salt to increase the ionic conductivity of the electrolyte. For example, if a pH of 1 is desired for the electrolyte, the concentration of acid may not be sufficient to provide good conductivity, so adding a salt may be preferred.

[0033] The electrolyte solution may be aqueous or non-aqueous. Suitable non-aqueous electrolyte solutions include acetone, sulfolane, dimethyl sulfoxide (DMSO), tetrahydrofuran (THF), dimethylformamide (DMF), N-methylpyrrolidone (NMP), hexamethylphosphoric acid triamide (HMPA), acetonitrile (MeCN), dichloromethane (DCM), propylene carbonate, hexafluoroisopropanol (HFIP), and the anion HSO4 - , CF3CO2 - , H2PO4- , Cl - , NO3 - , BF4 - , OTF - , PF6 - and ionic liquids (e.g., [C4mim] + etc.) In particular in embodiments in which the solvent is not an ionic liquid, the non-aqueous electrolyte solution preferably comprises an inorganic or organic salt as the electrolyte.

[0034] In order to increase the conversion rate of the furan compounds to HFOs and / or formylacrylic acid, the electrochemical oxidation is preferably carried out at a temperature in the range of 10 to 100°C, more preferably at a temperature in the range of 15 to 70°C. In particular, in electrochemical oxidation, it is not common to carry out oxidation at high temperatures (i.e., above room temperature). However, in the method of the present invention, it has been found that treatment at high temperatures, particularly at temperatures of about 35 to 60°C, improves the conversion rate and yield, and also improves solubility (i.e., allows for a somewhat higher concentration). When the furan compounds include furfural, the electrochemical oxidation of such furan compounds to HFOs and / or formylacrylic acid is preferably carried out at a temperature in the range of 20°C to 50°C in the presence of a mediator such as VO. In the absence of a mediator, a temperature of about room temperature (e.g., about 17 to 23°C) is preferred.

[0035] In chemical redox reactions, a higher concentration of starting material in the reaction solvent is generally favorable to obtain a high conversion rate, but in electrochemical oxidation reactions, this may not be the case because the conversion rate is limited by the electron density at the electrode and not so much by the concentration of reactants in the solution. In other words, the accessible electrode surface area and the current have a large effect on the conversion rate. In chemical redox reactions, a higher concentration of starting material in the reaction solvent is generally favorable to obtain a high conversion rate, but in electrochemical oxidation reactions, this may not be the case. In general, in such methods, increasing the concentration increases the current up to the value of the kinetic electrical current, the value of which depends on the nature of the electrode, the surface area of ​​the electrode, the molecules reacting, the adsorption characteristics on the electrode, etc. The reaction then does not proceed faster. It becomes limited by the exchange of products generated at the electrode with new reactants. In other words, the accessible electrode surface area, the current, and mass transfer generally have a large effect on the conversion rate. Therefore, a higher concentration does not necessarily increase the reaction rate, but rather increases the reaction time, which may lead to decomposition of reactants, intermediates, and products. This is particularly undesirable in continuous flow reactions, where complete conversion may not occur. Therefore, in embodiments in which the method includes electrochemical oxidation, it is preferred to carry out the electrochemical oxidation at a concentration of the furan compound in the electrolyte solution in the range of 0.01 to 5 mol / L, preferably in the range of 0.1 mol / L to 3.5 mol / L, more preferably in the range of 0.3 mol / L to 2 mol / L. Particularly good conversions and yields have been obtained in this range. The concentration may decrease over time, so the concentration here refers to the initial concentration of the furan compound, i.e., the concentration at the start of the reaction.

[0036] In a preferred embodiment, the electrochemical oxidation is carried out in two electrochemical cell compartments where the anode and cathode electrolyte solutions are separated by a membrane (e.g. a semi-permeable membrane such as a cation exchange membrane (CEM) or an anion exchange membrane (AEM) depending on the process characteristics). This embodiment is particularly preferred on a large scale since it can prevent the reaction products (i.e. HFO and / or formylacrylic acid) from being reduced at the cathode and also prevent or at least limit the crossover of furan compounds to the cathode, which would in either case reduce the efficiency. Membranes suitable for this embodiment include those available under the trade names Nafion™, Fumatech™, Neosepta™ and / or Selemion™. It can also be a porous diaphragm / glass frit.

[0037] Advantageously, the method may include counterelectrosynthesis to allow parallel electrochemical reduction at the cathode, such as the production of hydrogen from water, the reduction of oxygen to water, or the conversion of furfural to furfuryl alcohol. It may also be possible to reduce oxygen to water to reduce cell voltage and energy consumption.

[0038] It should be understood that the electrochemical oxidation of the present invention is particularly preferred for minimizing the generation of chemical waste. The generation of chemical waste can be further suppressed by carrying out the method of the present invention with an electrolyte solution consisting essentially of water, furan compounds, acids (as electrolyte), and possible reaction intermediates and products such as HFOs and / or formylacrylic acid. In other words, although possible, the presence of additives such as salts, stabilizers, buffers, surfactants, etc. is not preferred, and the electrolyte solution is preferably free of such additives. A further advantage of the electrolyte solution being free of salts is that the HFOs and / or formylacrylic acid are obtained directly as free acids, not necessarily as their salts. In step b), the free acids are generally preferred.

[0039] Instead of electrochemical oxidation, in step a) the furan compound can also be oxidized by photochemical reaction, as described, for example, by Galles et al. in Non-Patent Document 6. Such oxidation of furfural is described, for example, in Non-Patent Document 7 and Patent Document 2. Also, photochemical oxidation of 2-furoic acid is described, for example, in Non-Patent Document 8, Non-Patent Document 9, Non-Patent Document 10, Non-Patent Document 11 and Non-Patent Document 12.

[0040] The photochemical oxidation of furan compounds is preferably carried out in an organic solvent such as CHCl3, THF, or MeOH.

[0041] (Solvent for steps a) and b) If step a) is carried out in an aqueous electrolyte solution (this is preferred), step b) can be carried out in the same solution, in the same solution but after changing the pH, or in the same solution after extracting the HFO and / or formylacrylic acid with an organic solvent, preferably a water-immiscible organic solvent. In the latter embodiment, step b) is preferably carried out in the same type of organic solvent used for the extraction. It should be understood that this embodiment covers the method in which the organic extract is dried intermediately and the method in which it is not dried before further use. Examples of water-immiscible organic solvents that can be used include dichloromethane, toluene, ethyl acetate, 2-methyltetrahydrofuran, etc. In this particular embodiment, maleic anhydride may be obtained directly from the process without a separate subsequent dehydration step. Step b) may also be carried out in an alcoholic solvent, such as methanol or ethanol, to obtain the maleic acid monoester and / or maleic acid diester directly.

[0042] In embodiments of the present invention, the method includes steps a) and b) being carried out in the same solution, and further includes isolating maleic acid or its derivatives to provide isolated maleic acid or its derivatives and a spent electrolyte solution. The spent electrolyte solution can be recycled into the method. The spent electrolyte solution may include residual furan compounds, process intermediates, maleic acid, and other impurities and / or polymers produced. Therefore, it may be preferable to purify the spent electrolyte solution before recycling (e.g., nanofiltration to remove polymeric materials). Alternatively or in addition to purification, it may be preferable to release a portion of the recycled electrolyte and add fresh material to keep the quality of the electrolyte constant.

[0043] Isolation of maleic acid or its derivatives can be carried out using standard isolation techniques such as distillation. The specific isolation method that is preferred depends on the solvent used. Isolation of maleic acid can also return the pH of the electrolyte solution to its original pH, i.e., the pH at the start of the oxidation. Therefore, pH adjustment with additives may not be necessary. Note that if electrolyte, acid, solvent, or water is lost or consumed during the oxidation of the furan compounds or the isolation of maleic acid, the acid, solvent, and water can be replenished when recycling the electrolyte solution.

[0044] Recycling of the electrolyte solution is particularly preferred when the process is continuous, e.g., carried out in a continuous reaction system. The reaction system in which the process is carried out may optionally include a recycle loop for the electrolyte solution. Recycling of the electrolyte solution may provide the advantage of minimizing the generation of chemical waste and reducing external inputs.

[0045] Further embodiments of the present invention include a step of further reacting maleic acid. Derivatives of maleic acid obtained in the step of further reacting maleic acid may include fumaric acid, succinic acid, and their salts, esters, anhydrides, amides or imides. This optional further reaction step to provide maleic anhydride, fumaric acid, succinic acid or their salts, esters or anhydrides as is (i.e., without prior oxidation of the furan compound) is known in the art. For example, maleic anhydride, fumaric acid and succinic acid are obtained from maleic acid via dehydration, isomerization and partial hydrogenation, respectively. Fumaric acid is currently (mainly) produced industrially by catalytic isomerization of maleic acid. Succinic acid is also produced industrially by partial reduction of maleic acid, which is one of several known routes.

[0046] In a preferred embodiment of the invention, the method further comprises the step of isolating the maleic acid or a derivative thereof to provide an isolated maleic acid or a derivative thereof.

[0047] As used herein, the singular forms "a," "an," and "the" are intended to include the plural forms as well, unless the context clearly indicates otherwise. Additionally, the term "and / or" includes any and all combinations of one or more of the associated listed items. It should be understood that the terms "comprises" and / or "comprising" specify the presence of stated features but do not exclude the presence or addition of one or more other features.

[0048] Although for clarity and conciseness, features of the invention are described herein as part of the same or separate embodiments, it is to be understood that the scope of the invention includes embodiments having all or any combination of the described features. The present invention can be illustrated by the following non-limiting examples.

[0049] Example 1: Conversion of furfural to 5-hydroxy-2(5H)-furanone The anode compartment of the H-cell was filled with 100 mL of 0.5 M aqueous sulfuric acid solution containing 50 mM furfural. The conversion was carried out at 20 °C. The cathode compartment of the H-cell was filled with 100 mL of 0.5 M aqueous sulfuric acid solution. 10 cm 2 A PbO2 electrode was activated by CV between 0.5-2.1 V vs. SHE. A reference electrode and a working electrode were prepared, and a potential of 1.85 V vs. SCE was applied to the cell. Analysis showed that the ratio of the intermediates formylacrylic acid:maleic acid was about 2:1 after 7 hours, and about 9:1 after 20 hours. The maximum total yield of the products (maleic acid and 5-hydroxy-2(5H)-furanone) was about 80%.

[0050] Example 2 Extraction of cis-β-formylacrylic acid / 5-hydroxy-2(5H)-furanone and maleic acid from electrolyte An electrolyte containing approximately 1:10 ratio of formylacrylic acid:maleic acid was vigorously mixed with equal parts of organic solvents (ethyl acetate, dichloromethane, toluene, 2-methyltetrahydrofuran, diethyl ether) and the phases were separated. Both the aqueous and organic phases were analyzed by HPLC to determine the relative levels of cis-β-formylacrylic acid / 5-hydroxy-2(5H)-furanone and maleic acid in each phase.

[0051] [Table 1-1]

[0052] The ethyl acetate conditions were scaled up, and the organic and aqueous phases were separated, dried over sodium sulfate, and concentrated under reduced pressure to collect the product (400 mg) as a white solid, which was analyzed by NMR to determine a ratio of cis-β-formylacrylic acid / 5-hydroxy-2(5H)-furanone:maleic acid of approximately 2.7:1.

[0053] (Example 3) Conversion of furfural to 5-hydroxy-2(5H)-furanone Separate reactors were charged with the cis-β-formylacrylic acid / 5-hydroxy-2(5H)-furanone:maleic acid mixture (50 mg), 5% palladium on carbon (25 mg), and solvent (350 μL, either 0.5 M aqueous sulfuric acid or pH 7 aqueous buffer of monopotassium phosphate and dipotassium phosphate). The reactors were then heated to 70° C. with stirring, and oxygen was bubbled through the mixture. After 2 h, the reactions were cooled to room temperature and analyzed by HPLC. In all cases, conversion of cis-β-formylacrylic acid / 5-hydroxy-2(5H)-furanone to maleic acid was confirmed.

[0054] Example 4 Solvent for the Oxidation of HFO to Maleic Acid An autoclave (10 ml) was charged with HFO, solvent (1 ml) and 10% Pd / C according to Table 1-2 below.

[0055] The reactor was sealed and then flushed with nitrogen. The reactor was then filled with pure oxygen at a pressure of 10 bar. The reactor was then heated to 85°C and stirred for 15 hours. After cooling to ambient temperature, the pressure was released and the reactor was flushed with nitrogen. The product solution was filtered to remove the catalyst and then analyzed by high performance liquid chromatography (HPLC), and the yield of maleic acid was summarized in Table 1-2.

[0056] [Table 1-2] *TOF / sec of MA means the catalytic transition frequency of MA under those conditions.

[0057] Example 5: Catalyst for the oxidation of HFO to maleic acid in toluene An autoclave (10 ml) was charged with HFO (10.6 mg), toluene (1 ml) and catalyst according to Table 2. The reactor was sealed and then flushed with nitrogen. The reactor was then charged with pure oxygen at a pressure of 10 bar. The reactor was then heated to 111° C. and stirred for 14 h. After cooling to ambient temperature, the pressure was released and the reactor was flushed with nitrogen. The product solution was filtered to remove the catalyst and then analyzed by HPLC, the results of which are summarized in Table 2.

[0058] [Table 2] *TOF / sec of MA means the catalytic transition frequency of MA under those conditions.

[0059] (Additional Note) (Appendix 1) A method for preparing maleic acid or a derivative thereof, comprising the step of oxidizing 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid to maleic acid or a derivative thereof by contacting the 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid with molecular oxygen (O2) in the presence of a catalyst.

[0060] (Appendix 2) The catalyst is comprising a transition metal, metal salt, metal oxide or phosphate; Preferably, the metal constituting the catalyst is selected from the group consisting of cobalt, manganese, vanadium, molybdenum, copper, silver, gold, palladium, platinum and ruthenium; More preferably, the metal is gold. The method described in Appendix 1.

[0061] (Appendix 3) The catalyst is A solid support is included, Preferably, the carrier is selected from the group consisting of zirconia, silica, activated carbon, aluminum oxide, zinc oxide, and titanium dioxide; More preferably, the carrier is titanium dioxide or zirconia. 3. The method according to claim 1 or 2.

[0062] (Appendix 4) The method of any one of claims 1 to 3, wherein the 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid are liquid or dissolved in a solvent when contacted with O2.

[0063] (Appendix 5) The solvent is Contains an organic solvent or an aqueous solvent, Preferably, the solvent comprises a water-immiscible organic solvent or an acidic aqueous solvent. The method described in Appendix 4.

[0064] (Appendix 6) 6. The method according to any one of claims 1 to 5, wherein step b) is carried out under a pressure of at least 5 bar, preferably at least 10 bar.

[0065] (Appendix 7) 7. The method according to any one of claims 1 to 6, wherein step b) is carried out at a temperature in the range of from 20 to 200°C, preferably from 50 to 150°C, more preferably from 60 to 100°C.

[0066] (Appendix 8) 8. The method according to any one of claims 1 to 7, wherein step b) is carried out in a continuous reactor, preferably a tubular reactor.

[0067] (Appendix 9) The method of any one of claims 1 to 8, wherein step b) is preceded by a step of providing 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid as an isolated formulation.

[0068] (Appendix 10) 10. The method according to any one of claims 1 to 9, wherein the derivative of maleic acid is one or more selected from the group consisting of maleic anhydride, fumaric acid, succinic acid, succinonitrile, putrescine, malic acid, and salts, anhydrides, amides, imides or esters of any of these compounds.

[0069] (Appendix 11) the step (step b) of oxidizing 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid to maleic acid or a derivative thereof is preceded by a step a) of oxidizing a furan compound of formula I to 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid, [ka] R 1 is H, CHOH, COH or CHO, R 2 The method of any one of appendixes 1 to 10, wherein is H, OH, C1-C6 alkyl, or O(C1-C6 alkyl), or an ester, ether, amide, acid halide, anhydride, carboximidate, nitrile, and salt thereof.

[0070] (Appendix 12) 12. The method of claim 11, wherein step a) comprises electrochemically oxidizing the furan compound in an aqueous electrolyte solution, preferably comprising an acid, more preferably a mineral acid, even more preferably a mineral acid selected from the group consisting of hydrochloric acid (HCl), nitric acid (HNO3), phosphoric acid (H3PO4), sulfuric acid (H2SO4), boric acid (H3BO3), hydrofluoric acid (HF), hydrobromic acid (HBr), perchloric acid (HClO4), hydroiodic acid (HI), and most preferably sulfuric acid.

[0071] (Appendix 13) 13. The method of claim 12, wherein steps a) and b) are carried out in the same aqueous solution.

[0072] (Appendix 14) 13. The method of claim 12, wherein step a) is followed by an intermediate extraction step in which 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid are extracted with an organic solvent, and said step b) is carried out in the same organic solvent.

[0073] (Appendix 15) 15. The method of any one of claims 1 to 14, comprising converting maleic acid to one or more derivatives selected from the group consisting of maleic anhydride, fumaric acid, succinic acid, succinonitrile, putrescine, malic acid, and salts, anhydrides, amides, imides, or esters of any of these compounds.

Claims

1. 5-Hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid are reacted with molecular oxygen (O ２ b) oxidizing the maleic acid or a derivative thereof by contacting the maleic acid with the catalyst comprises a transition metal, a metal salt, a metal oxide, or a phosphate; The metal contained in the catalyst is selected from the group consisting of cobalt, manganese, vanadium, molybdenum, copper, silver, gold, palladium, platinum and ruthenium; A process for preparing maleic acid or its derivatives.

2. The metal is It is gold. The method of claim 1.

3. The catalyst is A solid support selected from the group consisting of zirconia, silica, activated carbon, aluminum oxide, zinc oxide, and titanium dioxide; The method according to claim 1 or 2.

4. 5-Hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid are ２ The method of any one of claims 1 to 3, wherein the compound is liquid or dissolved in a solvent when contacted with the compound.

5. The solvent is Contains an organic solvent or an aqueous solvent, The method according to claim 4.

6. The method according to any one of claims 1 to 5, wherein step b) is carried out under a pressure of at least 5 bar.

7. The method according to any one of claims 1 to 6, wherein step b) is carried out at a temperature in the range of from 20 to 200°C.

8. The process according to any one of claims 1 to 7, wherein step b) is carried out in a continuous reactor.

9. 9. The method according to any one of claims 1 to 8, wherein step b) is preceded by a step of providing 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid as isolated formulations.

10. 10. The method according to any one of claims 1 to 9, wherein the derivative of maleic acid is one or more selected from the group consisting of maleic anhydride, fumaric acid, succinic acid, succinonitrile, putrescine, malic acid, and the salts, anhydrides, amides, imides or esters of any of these compounds.

11. the step (step b) of oxidizing 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid to maleic acid or a derivative thereof is preceded by a step a) of oxidizing a furan compound of formula I to 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid, 【Chemistry 1】 R １ is H, CH ２ OH, CO ２ H or CHO, R ２ is H, OH, C １ -C ６ Alkyl or O(C １ -C ６ 11. The method of any one of claims 1 to 10, wherein the aryl group is a cyclic alkyl group, or an ester, ether, amide, acid halide, anhydride, carboximidate, nitrile, or salt thereof.

12. 12. The method of claim 11, wherein step a) comprises electrochemically oxidizing a furan compound in an aqueous electrolyte solution.

13. 13. The method of claim 12, wherein steps a) and b) are carried out in the same aqueous solution.

14. 13. The method of claim 12, wherein step a) is followed by an intermediate extraction step in which 5-hydroxy-2(5H)-furanone and / or cis-β-formylacrylic acid are extracted with an organic solvent, and said step b) is carried out in the same organic solvent.

15. 15. The method of any one of claims 1 to 14, comprising converting maleic acid to one or more derivatives selected from the group consisting of maleic anhydride, fumaric acid, succinic acid, succinonitrile, putrescine, malic acid, and the salts, anhydrides, amides, imides, or esters of any of these compounds.

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