WO2019014393A1

WO2019014393A1 - Novel processes for preparation of 2,5-furandicarboxylic acid

Info

Publication number: WO2019014393A1
Application number: PCT/US2018/041707
Authority: WO
Inventors: James M. Longmire; Stanley Herrmann; Eric L. Dias; Henricus Johannes Cornelis DEN OUDEN; Staffan Torssell; Ruja SHRESTHA; Gary M. Diamond
Original assignee: Stora Enso Oyj
Current assignee: Stora Enso Oyj
Priority date: 2017-07-12
Filing date: 2018-07-11
Publication date: 2019-01-17
Anticipated expiration: 2020-01-12
Also published as: TW201917123A

Abstract

La présente invention concerne des procédés de production d'acide 2,5-furandicarboxylique (FDCA) à partir de divers substrats, comprenant des acides C6-aldariques et des lactones d'acides C6-aldariques. The present invention relates to processes for producing 2,5-furandicarboxylic acid (FDCA) from various substrates, including C6-aldaric acids and C6-aldaric acid lactones.

Description

NOVEL PROCESSES FOR PREPARATION OF 2,5-FURANDICARBOXYLIC ACID

PARTIES OF JOINT RESEARCH AGREEMENT

[0001] The subject matter disclosed and the claimed invention was made by, or on behalf of, and/or in connection with a joint research agreement between Rennovia Inc. and Stora Enso Oyj that was in effect on and before the date the claimed invention was made, and the claimed invention was made as a result of activities undertaken within the scope of the agreement.

FIELD

[0002] Aspects of the present disclosure relate to processes for preparing 2,5- furandicarboxylic acid from various substrates, including C₆-aldaric acids and lactones of C₆- aldaric acids.

BACKGROUND

[0003] Low cost, renewably-derived 2,5-furandicarboxylic acid (FDCA) and its derivatives have many commercial applications. For instance, FDCA and its derivatives have the potential to displace aromatic dicarboxylic acids such as terephthalic and isophthalic acid. FDCA and its derivatives are also useful in the production of other commodity chemicals. For example, FDCA may be hydrogenated to adipic acid, which is utilized in the production of nylon. Aromatic dicarboxylic acids are used for the production of polyesters and polyamides in the scale of tens of millions of tons per year.

[0004] FDCA can be produced by direct oxidation of 5-hydroxymethylfurfural (HMF) with nitric acid, though with low selectivity and yield. FDCA and its esters can be produced by oxidation of mono- or dialkoxymethylfurfural in the presence of a homogeneous catalytic system that is similar to the system used in terephthalic acid production (Co/Mn/Br) and results a maximum total yield of furandicarboxylics (with FDCA as a major constituent) of 82%. Despite the availability of these processes, a significant need exists for processes that can produce FDCA in higher yields and in large quantities, particularly from readily available biological feedstocks, to realize the potential of FDCA as a biorenewable-derived replacement for petroleum-derived compounds in the production of plastics and other materials.

SUMMARY

[0005] In one aspect, the present disclosure is directed to a process for producing

2.5- furandicarboxylic acid (FDCA), the process comprising contacting a sugar derivative substrate with a Bronsted acid and a halide salt in the presence of a water-miscible organic solvent to form a reaction mixture, and producing FDCA.

[0006] The sugar derivative substrate can be a homogeneous sugar derivative substrate or the sugar derivative substrate can be a heterogeneous sugar derivative substrate. The sugar derivative substrate can be selected from the group consisting of glucaric acid, glucaric acid dilactone, 1,4-glucaric acid monolactone, 3,6-glucaric acid monolactone, sodium glucarate, potassium glucarate, calcium glucarate, galactaric acid, 1,4-galactaric acid monolactone, 3,6-galactaric acid monolactone, sodium galactarate, potassium galactarate, calcium galactrate, mannaric acid, mannaric acid dilactone, 1,4-mannaric acid monolactone,

3.6- mannaric acid monolactone, sodium mannarate, potassium mannarate, calcium mannarate, or a mixture thereof.

[0007] The Bronsted acid can selected from the group consisting of hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, phosphoric acid, methanesulfonic acid, p-toluenesulfonic acid, benzenesulfonic acid, trifluoromethanesulfonic acid, acetic acid, and trifluoracetic acid. The Bronsted acid can be selected from the group consisting of hydrochloric acid, hydrobromic acid, sulfuric acid, and methanesulfonic acid.

[0008] The halide salt can be a metal halide or a tetraalkylammonium halide. The metal halide can be selected from the group consisting of FeBr₂, FeBr₃, FeCl₂, FeCl₃, CuBr, CuBr₂, CuCl, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, NaCl, NaBr, Nal, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, MgBr₂, KC1, KBr, and KI. The metal halide salt can be selected from the group consisting of FeBr₂, FeCl₂, CuBr₂, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, and MgBr₂. The metal halide salt can be CaBr₂ and the Bronsted acid can be hydrobromic acid. The metal halide salt can be CaBr₂ and the Bronsted acid can be hydrochloric acid. The metal halide salt can be CaBr₂ and the Bronsted acid can be methanesulfonic acid. The metal halide salt can be CaBr₂ and the Bronsted acid can be sulfuric acid. The metal halide salt can be MgBr₂ and the Bronsted acid can be hydrobromic acid. The metal halide salt can be MgBr₂ and the Bronsted acid can be methanesulfonic acid. The metal halide can be MgBr₂ and the Bronsted acid can be sulfuric acid. The metal halide can be LiBr and the Bronsted acid can be hydrobromic acid. The metal halide can be LiBr and the Bronsted acid can be methanesulfonic acid. The metal halide salt can be ZnCl₂ and the Bronsted acid can be hydrochloric acid.

[0009] The tetraalkylammonium halide can be selected from the group consisting of tetramethylammonium chloride, tetramethylammonium bromide, tetraethylammonium chloride, tetraethylammonium bromide, tetrabutylammonium chloride, and tetrabutylammonium bromide. The tetraalkylammonium halide salt can be tetraethylammonium bromide and the Bronsted acid can be methanesulfonic acid.

[0010] The water-miscible organic solvent can be selected from the group consisting of 1,4-dioxane, tetrahydrofuran, sulfolane, a glyme, N-methyl-2-pyrrolidone, methyl ethyl ketone, dimethyl foimamide, and dimethyl sulfoxide. The water-miscible organic solvent can be 1,4-dioxane or sulfolane. The glyme can be selected from the group consisting of 1,2-dimethoxyethane, ethyl glyme, diethylene glycol dimethyl ether, ethyl diglyme, triglyme, butyl diglyme, tetraglyme, and a polyglyme.

[0011] The reaction mixture can be pressurized to a pressure ranging from 15-500 psi, 25-500 psi, 50-500 psi, 100-500 psi, 200-500 psi, 300-500 psi, or 400-500 psi or can be within a range defined by any two of the aforementioned pressures.

[0012] The concentration of the sugar derivative substrate can be in the range from 0.01 M to 10.0 M. The concentration of acid can range from between 0.01-10.0 M, 0.02-5.0 M, 0.05-2.0 M, 0.10-1.0 M, 0.15-1.0 M, 0.20-1.0 M, 0.2-1.25 M, 0.4-1.25 M, 0.5- 1.0 M, or 0.6-1.25 M, or can be within a range defined by any two of the aforementioned concentrations.

[0013] The concentration of Bronsted acid can be in the range from 0.05 M to 10.0 M. The concentration of acid can range from between 0.05-10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or can be within a range defined by any two of the aforementioned concentrations.

[0014] The concentration of halide salt can range from between 0.01-3.0 M, 0.05- 2.0 M, 0.1-1.0 M, or 0.2-0.5 M, or can be within a range defined by any two of the aforementioned concentrations. The concentration of halide salt can be at least 0.1 M. The concentration of halide salt can be less than 2.0 M, or less than 1.5 M, or less than 1 M, or less than 0.75 M, or less than 0.5 M but not zero.

[0015] The process can further comprise adding water to the reaction mixture. The concentration of water can range from between 0.01- 20.0 M, 0.01- 10.0 M, 0.1-5.0 M, or 0.2-1.0 M, or can be within a range defined by any two of the aforementioned concentrations.

[0016] The process can further comprise adding alcohol to the reaction mixture. The alcohol can be selected from the group consisting of n-butanol, sec-butanol, isobutanol, 1-pentanol, 2-pentanol, 2-(2-chloroethoxy) ethanol), ethoxyethanol, and cyclohexanol. The concentration of alcohol can range from between 0.01-1.0 M, 0.1-l.OM, or 0.5-1.0M, or can be within a range defined by any two of the aforementioned concentrations.

[0017] The process can comprise the step of pressurizing the reaction mixture with one or more gasses selected from the group consisting of nitrogen, argon, helium, and carbon dioxide.

[0018] The process can comprise the step of heating the reaction mixture. The reaction mixture can be heated to a temperature range from between 90-200 °C, 110-160 °C, 110-180 °C, 70-150 °C, 80-150 °C, 90-150 °C, 100-150 °C, 110-150 °C, 120-150 °C, 130-150 °C, or 140-150 °C or within a range defined by any two of the aforementioned temperatures. The reaction mixture can be heated to a temperature of 90 °C. The reaction mixture can be heated to a temperature of 120 °C. The reaction mixture can be heated to a temperature of 140 °C or 160 °C. The reaction mixture can be heated for 1 min. to 24 hours, 1 min. to 3 hours, 1 min. to 0.5 hours, 0.5-96 hours, 1-96 hours, 2-72 hours, 5-48 hours, 1-24 hours, 2-24 hours, 12-24 hours, or 20-24 hours or for a time that is within a range defined by any two of the aforementioned times. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times. [0019] The concentration of sugar derivative substrate can range from between 0.05-10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or can be within a range defined by any two of the aforementioned concentrations.

[0020] The process for producing FDCA can result in formation of 2-furoic acid.

[0021] The process for producing FDCA may utilize dioxane as the water- miscible organic solvent, and the process can further comprise: forming a 2-haloethoxy ethanol; and reacting the 2-haloethoxy ethanol with FDCA to form a mono- or di-ester of FDCA. The process can further comprise hydrolyzing the FDCA ester with a base to form an FDCA salt. The base can be selected from the group consisting of NaOH, KOH, LiOH, Ca(OH)₂, and CsOH.

[0022] The process for producing FDCA can further comprise preparing the sugar derivative substrate from lignocellulosic material by subjecting the lignocellulosic material to hydrolysis conditions followed by oxidation conditions to produce a sugar derivative substrate. The hydrolysis of the lignocellulosic material can produce a sugar derivative substrate comprising a mixture of C₆-aldaric acids. The lignocellulosic material may comprise a compound selected from the group consisting of cellulose, hemicellulose, and lignin.

[0023] The yield of FDCA for the process can be at least 60%, or at least 70%, or at least 80%, or at least 90%, or at least 95%, or at least 98%, or at least 99% or within a range defined by any two of the aforementioned percentages. The yield of FDCA can be at least 60%, or at least 70%, or at least 80%, or at least 90%, or at least 95%, or at least 98%, or at least 99% or within a range defined by any two of the aforementioned percentages.

[0024] The process for producing FDCA can produce FDCA and additional impurities. The amount of FDCA relative to the additional impurities can be at least 60%, or at least 65%, or at least 70%, or at least 75%, or at least 80%, or at least 85%, or at least 90%, or at least 91%, or at least 92%, or at least 93%, or at least 94%, or at least 95%, or at least 96%, or at least 97%, or at least 98%, or at least 99% by weight percent, or within any range defined by the aforementioned weight percents. The molar ratio of FDCA to 2-furoic acid can be least 5:1, or at least 6:1 or at least 7:1, or at least 8:1, or at least 9:1, or at least 10:1, or at least 15:1, or at least 20:1, or at least 25:1, or at least 30:1, or at least 35:1, or at least 40:1, or at least 45:1, or at least 50:1, or within any range defined by the aforementioned molar ratios.

[0025] The process for producing FDCA can further comprise steps of isolating, crystalizing, or decolorizing said FDCA.

[0026] In another aspect, the present disclosure is directed to reaction mixture comprising: a sugar derivative substrate; a water-miscible organic solvent; a halide salt; and a Bronsted acid. The reaction mixture can further comprise FDCA.

[0027] The sugar derivative substrate can be a homogenous sugar derivative substrate. The sugar derivative substrate can be a heterogeneous sugar derivative substrate. The sugar derivative substrate can be selected from the group consisting of: glucaric acid and salts and lactones thereof; galactaric acid and salts and lactones thereof; and mannaric acid and salts and lactone thereof; or a mixture thereof. The sugar derivative substrate can be selected from the group consisting of glucaric acid, glucaric acid dilactone, 1,4-glucaric acid monolactone, 3,6-glucaric acid monolactone, sodium glucarate, potassium glucarate, calcium glucarate, galactaric acid, 1,4-galactaric acid monolactone, 3,6-galactaric acid monolactone, sodium galctarate, potassium galactarate, calcium galactarate, mannaric acid, mannaric acid dilactone, 1,4-mannaric acid monolactone, 3,6-mannaric acid monolactone, sodium mannarate, potassium mannarate, calcium mannarate, or a mixture thereof. The sugar derivative substrate can be glucaric acid, or a salt or lactone thereof. The sugar derivative substrate can be galactaric acid, or a salt or lactone thereof. The sugar derivative substrate can be mannaric acid, or a salt or lactone thereof. The sugar derivative substrate can be glucaric acid dilactone. The sugar derivative substrate can be mannaric acid dilactone.

[0028] The concentration of sugar derivative substrate in the mixture can range from between 0.05-10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or can be within a range defined by any two of the aforementioned concentrations.

[0029] The water-miscible organic solvent can be selected from the group consisting of 1,4-dioxane, tetrahydrofuran, sulfolane, a glyme, N-methyl-2-pyrrolidone, methyl ethyl ketone, dimethyl foimamide, and dimethyl sulfoxide. The water-miscible organic solvent can be 1,4-dioxane or sulfolane.

[0030] The Bronsted acid can be selected from the group consisting of hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, phosphoric acid, methanesulfonic acid, p-toluenesulfonic acid, benzenesulfonic acid, trifluoromethanesulfonic acid, acetic acid, and trifluoracetic acid.

[0031] The concentration of the acid in the mixture can range from between 0.05- 10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or within a range defined by any two of the aforementioned concentrations.

[0032] The halide salt can be a metal halide or a tetraalkylammonium halide. The metal halide can be selected from the group consisting of FeBr₂, FeBr₃, FeCl₂, FeCl₃, CuBr, CuBr₂, CuCl, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, NaCl, NaBr, Nal, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, MgBr₂, KC1, KBr, and KI. The metal halide salt can be selected from the group consisting of FeBr₂, FeCl₂, CuBr₂, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, and MgBr₂. The metal halide salt can be CaBr₂ and the Bronsted acid can be hydrobromic acid. The metal halide salt can be CaBr₂ and the Bronsted acid can be hydrochloric acid. The metal halide salt can be CaBr₂ and the Bronsted acid can be methanesulfonic acid. The metal halide salt can be CaBr₂ and the Bronsted acid can be sulfuric acid. The metal halide salt can be MgBr₂ and the Bronsted acid can be hydrobromic acid. The metal halide salt can be MgBr₂ and the Bronsted acid can be methanesulfonic acid. The metal halide can be MgBr₂ and the Bronsted acid can be sulfuric acid. The metal halide can be LiBr and the Bronsted acid can be hydrobromic acid. The metal halide can be LiBr and the Bronsted acid can be methanesulfonic acid. The metal halide salt can be ZnCl₂ and the Bronsted acid can be hydrochloric acid.

[0033] The tetraalkylammonium halide can be selected from the group consisting of tetramethylammonium chloride, tetramethylammonium bromide, tetraethylammonium chloride, tetraethylammonium bromide, tetrabutylammonium chloride, and tetrabutylammonium bromide. The tetraalkylammonium halide salt can be tetraethylammonium bromide and the Bronsted acid can be methanesulfonic acid.

[0034] The water-miscible organic solvent can be selected from the group consisting of 1,4-dioxane, tetrahydrofuran, sulfolane, a glyme, N-methyl-2-pyrrolidone, methyl ethyl ketone, dimethyl formamide, and dimethyl sulfoxide. The water-miscible organic solvent can be 1,4-dioxane or sulfolane. The glyme can be selected from the group consisting of 1,2-dimethoxyethane, ethyl glyme, diethylene glycol dimethyl ether, ethyl diglyme, triglyme, butyl diglyme, tetraglyme, and a polyglyme. [0035] The concentration of halide salt in the mixture can range from between 0.01-3.0 M, 0.05-0.2 M, 0.1-1.0 M, or 0.2-0.5 M, or can be within a range defined by any two of the aforementioned concentrations. The concentration of halide salt can be at least 0.1 M. The concentration of halide salt can be less than 2.0 M, or less than 1.5 M, or less than 1 M, or less than 0.75 M, or less than 0.5 M but not zero.

[0036] The reaction mixture can further comprise water. The concentration of water in the mixture can range from between 0.01-20.0 M, 0.01- 10.0 M, 0.1-5.0 M, or 0.2- 1.0 M, or can be within a range defined by any two of the aforementioned concentrations.

[0037] The reaction mixture can further comprise an alcohol. The alcohol can be selected from the group consisting of n-butanol, sec-butanol, isobutanol, 1-pentanol, 2- pentanol, 2-(2-chloroethoxy) ethanol), ethoxyethanol, and cyclohexanol. The concentration of alcohol ranges from between 0.01-1.0 M, 0.1-l.OM, or 0.5-1.0M, or within a range defined by any two of the aforementioned concentrations.

[0038] The reaction mixture can comprise compounds derived from the hydrolysis of cellulose, hemicellulose, or lignin. The reaction mixture can comprise 2-furoic acid.

BRIEF DESCRIPTION OF THE FIGURES

[0039] Figure 1A depicts 2,5-furandicarboxylic acid (FDCA) and 2-furoic acid (2-FA) yields in sulfolane using a variety of halide salts and and in the absence of a Bronsted acid.

[0040] Figure IB depicts FDCA and 2-FA yields in sulfolane in the presence of HBr as a Bronsted acid using a variety of halide salts.

[0041] Figure 1C depicts FDCA and 2-FA yields in sulfolane in the presence of HC1 as a Bronsted acid using a variety of halide salts.

[0042] Figure ID depicts FDCA and 2-FA yields in sulfolane in the presence of H₂S0₄ as a Bronsted acid using a variety of halide salts.

[0043] Figure IE depicts FDCA and 2-FA yields in sulfolane in the presence of MsOH as a Bronsted acid using a variety of halide salts.

[0044] Figure IF depicts FDCA and 2-FA yields in sulfolane in the presence of F3CSO3H as a Bronsted acid using a variety of halide salts. [0045] Figure 2A depicts FDCA selectivity versus conversion for glucaric acid dilactone (GADL) substrate in sulfolane using a variety of halide salts and and in the absence of a Bronsted acid.

[0046] Figure 2B depicts FDCA selectivity versus conversion for GADL substrate in sulfolane in the presence of HBr as a Bronsted acid using a variety of halide salts.

[0047] Figure 2C depicts FDCA selectivity versus conversion for GADL substrate in sulfolane in the presence of HC1 as a Bronsted acid using a variety of halide salts.

[0048] Figure 2D depicts FDCA selectivity versus conversion for GADL substrate in the presence of H₂S0₄ as a Bronsted acid using a variety of halide salts.

[0049] Figure 2E depicts FDCA selectivity versus conversion for GADL substrate in the presence of MsOH as a Bronsted acid using a variety of halide salts.

[0050] Figure 2F depicts FDCA selectivity versus conversion for GADL substrate in the presence of F3CSO3H as a Bronsted acid using a variety of halide salts.

[0051] Figure 3A depicts FDCA yield from GADL in sulfolane with Bronsted acid concentrations in the range of about 7 M to about 6 M using a variety of halide salts.

[0052] Figure 3B depicts FDCA yield from GADL in sulfolane with Bronsted acid concentrations of about 5 M using a variety of halide salts.

[0053] Figure 3C depicts FDCA yield from GADL in sulfolane with Bronsted acid concentrations of about 4 M using a variety of halide salts.

[0054] Figure 3D depicts FDCA yield from GADL in sulfolane with Bronsted acid concentrations of about 3 M using a variety of halide salts.

[0055] Figure 3E depicts FDCA yield from GADL in sulfolane with Bronsted acid concentrations of about 2 M using a variety of halide salts.

[0056] Figure 3F depicts FDCA yield from GADL in sulfolane with Bronsted acid concentrations in the range of about 1 M to about 0 M using a variety of halide salts.

[0057] Figure 4 depicts FDCA yield from GADL in sulfolane as a function of halide salt and Bronsted acid concentrations at different temperatures.

[0058] Figure 5 depicts the mass balance and yields of 2-FA from the reaction of GADL sugar derivative substrate in sulfolane. [0059] Figure 6 depicts FDCA yield and conversion from GADL with CaBr₂ and H₂S0₄ selected as the halide salt and Bronsted acid, respectively in sulfolane at different H₂0 concentrations.

[0060] Figure 7 depicts a comparison of FDCA yield from GADL with CaBr₂ or MgBr₂ in sulfolane using different sources of Bronsted acid and different H₂0 concentrations.

[0061] Figure 8 depicts FDCA yield from GADL with CaBr₂ or MgBr₂ in sulfolane as a function of the ratio of halide salt concentration to acid concentration at different H₂0 concentrations.

[0062] Figure 9 depicts the mass balance and yields of 2-FA from the reaction of GADL sugar derivative substrate with CaBr₂ or MgBr₂ in sulfolane at different H₂0 concentrations.

[0063] Figure 10 depicts FDCA yield and selectivity using GADL as the sugar derivative substrate in sulfolane.

[0064] Figure 11 A depicts FDCA selectivity as a function of the ratio of halide concentration to proton concentration as well as FDCA yield versus conversion of GADL sugar derivative substrate using CaBr₂ as a halide salt.

[0065] Figure 1 IB depicts FDCA selectivity as a function of the ratio of halide concentration to proton concentration as well as FDCA yield versus conversion of GADL sugar derivative substrate using LiBr as a halide salt.

[0066] Figure 11C depicts FDCA selectivity as a function of the ratio of halide concentration to proton concentration as well as FDCA yield versus conversion of GADL sugar derivative substrate using MgBr₂ as a halide salt.

[0067] Figure 1 ID depicts FDCA selectivity as a function of the ratio of halide concentration to proton concentration as well as FDCA yield versus conversion of GADL sugar derivative substrate in the absence of a halide salt.

[0068] Figure 12 depicts yields of 2-FA and mass balance using GADL as the sugar derivative substrate in sulfolane in HC1 and HBr systems as a function of the ratio of halide salt concentration to acid concentration. [0069] Figure 13 depicts FDCA yield both as a function of Bronsted acid concentration and conversion of GADL in sulfolane when no halide salt is added to the reaction.

[0070] Figure 14 depicts the yield of FDCA versus conversion of GADL in dioxane using various Bronsted acids and in the absence of halide salts at a variety of water concentrations.

[0071] Figure 15 depicts the selectivity of FDCA formation from GADL versus the conversion of FDCA in dioxane using various Bronsted acids and in the absence of halide salts at a variety of water concentrations.

[0072] Figure 16 depicts the yield of FDCA versus conversion of GADL in NMP using various Bronsted acids and in the absence of halide salts at a variety of water concentrations.

[0073] Figure 17 depicts the selectivity of FDCA formation from GADL versus the conversion of FDCA in NMP using various Bronsted acids and in the absence of halide salts at a variety of water concentrations.

[0074] Figure 18 depicts the selectivity of FDCA formation from GADL in dioxane versus the concentration of TEAB added to the reaction mixture.

[0075] Figure 19 depicts the conversion of GADL in dioxane/HCl and dioxane/HBr versus the concentration of TEAB added to the reaction mixture.

[0076] Figure 20 depicts the yield of FDCA versus conversion of GADL in dioxane/HCl and a variety of water concentrations versus the concentration of TEAB added to the reaction mixture.

[0077] Figure 21 depicts the yield of 2-FA versus conversion of GADL in dioxane/HCl and a variety of water concentrations versus the concentration of TEAB added to the reaction mixture.

[0078] Figure 22 depicts the conversion of GADL in dioxane/HCl and a variety of water concentrations versus the concentration of TEAB added to the reaction mixture.

[0079] Figure 23 depicts the yield of FDCA from GADL in dioxane/HCl and a variety of water concentrations versus the concentration of TEAB added to the reaction mixture. [0080] Figure 24 depicts the yield of 2-FA from GADL in dioxane/HCl and a variety of water concentrations versus the concentration of TEAB added to the reaction mixture.

[0081] Figure 25 depicts the yield of FDCA from GADL in dioxane/HCl and a variety of water concentrations versus the concentration of tetraethylammonium chloride (TEAC) added to the reaction mixture.

[0082] Figure 26 depicts the yield of 2-FA from GADL in dioxane/HCl and a variety of water concentrations versus the concentration of TEAC added to the reaction mixture

[0083] Figure 27 depicts the conversion of GADL, yields of FDCA and 2-FA and selectivity for FDCA in dioxane/HCl and TEAB versus the concentration of acid in the reaction mixture.

DETAILED DESCRIPTION

I. Definitions

[0084] Unless defined otherwise, all technical and scientific terms used herein have the same meaning as is commonly understood by one of ordinary skill in the art. All patents, applications, published applications and other publications referenced herein are expressly incorporated by reference in their entireties unless stated otherwise. In the event that there are a plurality of definitions for a term herein, those in this section prevail unless stated otherwise.

[0085] As used herein, the term "sugar derivative substrate" refers to a composition comprising one or more compounds selected from C₆-aldaric acids, and/or lactones, esters and/or salts of C₆-aldaric acids. Examples of sugar derivative substrates include but are not limited to e.g., glucaric acid, sodium glucarate, potassium glucarate, calcium glucarate, glucaric acid 1,4-monolactone, glucaric acid 3,6-monolactone, glucaric acid dilactone, galactaric (mucic) acid, sodium galactarate, potassium galactarate, calcium galactarate, galactaric acid 1,4-monolactone, galactaric acid 3,6-monolactone, mannaric acid, sodium mannarate, potassium mannarate, calcium mannarate, mannaric acid 1,4- monolactone, mannaric acid 3,6-monolactone, and/or mannaric acid dilactone. The sugar derivative substrate may be homogenous or heterogenous. A homogenous sugar derivative substrate contains a single species of a C₆-aldaric acid, or a single species of a lactone, ester, or salt of a C₆-aldaric acid. A heterogenous sugar derivative substrate contains two or more species of C₆-aldaric acids, or lactones, esters, or salts of C₆-aldaric acid.

[0086] As used herein the term "C₆-aldaric acid" refers to a compound having the formula HOOC-(CHOH)₄-COOH, or a salt thereof. Examples of C₆-aldaric acids include glucaric acid, galctaric acid, mannaric acid and/or gularic acid. C₆-aldaric acids may be derived from sugars, and/or may be obtained, for example, by oxidation of aldoses.

[0087] As used herein, the term "Bronsted acid" refers to a compound that acts as a proton donor. Bronsted acids include but are not limited to e.g., hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, nitric acid, phosphoric acid, acetic acid, trifluoracetic acid, formic acid, methanesulfonic acid, p-toluenesulfonic acid, benzenesulfonic acid, and/or trifluoromethanesulfonic acid.

[0088] As used herein the term "halide salt" refers to an ionic compound composed of cations and halide anions (e.g., F^", CI^", Br^", and Γ). Halide salts may have a metal cation, including, but not limited to e.g., Li⁺, Na⁺, K⁺, Ca²⁺, Mg²⁺, Cu²⁺, Cu³⁺, Fe²⁺, Fe³⁺, Zn²⁺, and/or Ni²⁺. Halide salts may have a tetraalkylammonium cation of the formula NR-f^1", where each R is independently selected from a C_1-8 alkyl. Tetraalkylammonium halide salts include, but are not limited to e.g., tetramethylammonium, tetraethylammonium, and/or tetrabutylammonium. Exemplary halide salts include but are not limited to e.g., LiCl, LiBr, Lil, NaCl, NaBr, Nal, KF, KC1, KBr, KI, CaCl₂, CaBr₂, MgCl₂, MgBr₂, CuCl, CuCl₂, CuBr, CuBr₂, FeCl₂, FeCl₃, FeBr₂, FeBr₃, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, tetramethylammonium choride, tetramethylammonium bromide, tetramethylammonium iodide, tetraethylammonium chloride, tetraethylammonium bromide, tetraethylammonium iodide, tetrabutylammonium chloride, tetrabutylammonium bromide, and/or tetrabutylammonium iodide.

[0089] As used herein, the term "water-miscible organic solvent" refers to a carbon-containing compound that forms a homogenous mixture when mixed with water at room temperature. Examples of water-miscible organic solvents include but are not limited to e.g., 1,4-dioxane, tetrahydrofuran (THF), sulfolane, N-methyl-2-pyrrolidinone (NMP), dimethylfoimamide (DMF), dimethylsulfoxide (DMSO), methyl ethyl ketone, acetic acid, ethanol, «-propanol, 1,3 -propanediol, isopropanol, «-butanol, 1,2-butanediol, 1,3-butanediol, I, 4-butanediol, 1,5-pentanediol, acetonitrile, ethylene glycol, propylene glycol, pyridine, and/or a glyme.

[0090] As used herein, the term "glyme" refers to alkyl ethers of ethylene glycol or propylene glycol. Examples of glymes include but are not limited to e.g., 1,2- dimethoxyethane, ethyl glyme, diethylene glycol dimethyl ether, ethyl diglyme, triglyme, butyldiglyme, tetraglyme, and/or a polyglyme.

[0091] As used herein, the term "alcohol" refers to a compound comprising a Ci_ 20 straight, branched, or cyclic chain bearing one or more hydroxyl (-OH) groups. The C_1-2o chain may optionally comprise one or more C-C double or C-C triple bonds. The Ci-2o chain may also be optionally substituted with one or more groups selected from halogens (e.g., -F, -CI, -Br, or -I), -O-Ci^oalkyl, and/or -O-Ci^ohaloalkyl. Examples of alcohols include but are not limited to e.g., methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, t- butyl alcohol, 2,2,2-trifluoroethanol, hexafluoro-2-propanol, cylcopentanol, cyclohexanol, methoxyethanol, ethoxyethanol, and/or 2-(2-chloroethoxy)ethan-l-ol (CEE).

[0092] As used herein, the term "lignocellulosic material" refers to a composition comprising cellulose, hemicellulose, and/or lignin. Lignocellulosic material may be derived from a variety of sources including, but not Umited to e.g., logs, whole tree chips, bark chips, hybrid poplar, hybrid willow, sawdust, pulp waste, paper pulp, soybeans, sugar beets, sugarcane, bagasse, corn, corn stover, switchgrass, wheat, plant biomass, agricultural waste, and/or plant-derived household waste.

[0093] As used in this specification, whether in a transitional phrase or in the body of the claim, the terms "comprise(s)" and "comprising" are to be interpreted as having an open-ended meaning. That is, the terms are to be interpreted synonymously with the phrases "having at least" or "including at least." When used in the context of a process, the term "comprising" means that the process includes at least the recited steps, but may include additional steps. When used in the context of a compound, composition or device, the term "comprising" means that the compound, composition or device includes at least the recited features or components, but may also include additional features or components.

II. Producing sugar derivative substrates from lignocellulosic material

[0094] Lignocellulosic material may be processed to produce a sugar derivative substrate. In some embodiments, the lignocellulosic material may be derived from one or more sources including but not limited to e.g., logs, whole tree chips, bark chips, hybrid poplar, hybrid willow, sawdust, pulp waste, paper pulp, soybeans, sugar beets, sugarcane, bagasse, corn, corn stover, switchgrass, wheat, plant biomass, agricultural waste, and/or plant-derived household waste.

[0095] In some embodiments, lignocellulosic material may be subjected to hydrolysis conditions with or without separation (e.g., chromatographic separation) followed by oxidation conditions to produce a sugar derivative substrate. Methods of converting lignocellulosic material to a sugar derivative substrate were previously described by Rennovia in WO2011/155964 to Murphy et al., which is hereby expressly incorporated herein by reference in its entirety. Additional methods for converting lignocellulosic material to a sugar derivative substrate have been described in EP3088377 and EP3088378, both to Marion et al., which are also hereby expressly incorporated by reference in their entireties.

[0096] The hydrolysis conditions for the lignocellulosic material are not limited to a specific method. In one embodiment, the lignocellulosic material may be subjected to chemical hydrolysis conditions. Chemical hydrolysis of lignocellulosic material may be readily achieved by treating the material with an aqueous acid, such as aqueous H₂S0₄ or HC1. In one embodiment, lignocellulosic material may be subjected to enzymatic hydrolysis conditions. In some embodiments, the lignocellulosic material is subjected to hydrolysis conditions that produces C₆-aldoses. In some embodiments, the lignocellulosic material is subjected to hydrolysis conditions that produce glucose.

[0097] The hydrolyzed material may be oxidized to produce a sugar derivative substrate by any one of several available methods. In some embodiments, the hydrolyzed material is filtered to remove particulate matter before being subjected to oxidation conditions. In one embodiment, the hydrolyzed material is oxidized using nitric acid. In some embodiments, oxidation of the hydrolyzed material may be achieved by oxidizing an aqueous solution of the hydrolyzed material with oxygen in the presence of an oxidation catalyst. The oxygen can be supplied to the reaction as air, oxygen enriched air, oxygen alone, or oxygen with other constituents substantially inert to the reaction. The oxidation may comprise at least one noble metal, including but not limited to e.g., Au, Pt and/or Pd, and may further comprise a solid support, such as a carbon, ceria, titania or a zirconia support. Exemplary oxidation catalysts include Pd/C, Au-Pt/ZrC<2 and/or Au-Pt/TiCh. In some embodiments, the oxidation catalysts are selected from the catalysts described by Rennovia in WO2011/155964 to Murphy et al. In some embodiments, the oxidation conditions are conducted in the presence of a base. In some embodiments, the oxidation conditions are conducted in the absence of added base.

[0098] In some embodiments, the lignocellulosic material is subjected to hydrolysis conditions followed by oxidation conditions to produce C₆-aldaric acids. The resulting C₆-aldaric acids may be converted to the corresponding lactones, esters, or salts by appropriate methods referenced by Rennovia in WO2011/155964 to Murphy et al. For example, with respect to lactones, without wishing to be bound by theory, it is believed that various mono- and di-lactones are present in equilibrium with aldaric acids in aqueous solution. In some embodiments, the lignocellulosic material is subjected to hydrolysis conditions followed by oxidation conditions to produce glucaric acid. The resulting glucaric acid may be converted to a corresponding lactone, ester, or salt by appropriate methods referenced by Rennovia in WO2011/155964 to Murphy et al. In some embodiments, the lignocellulosic material is subjected to hydrolysis to produce mannaric acid, which may subsequently be converted to a corresponding lactone, ester, or salt.

ΙΠ. Dehydration of sugar derivative substrates to produce FDCA

[0099] In some embodiments provided herein, the present disclosure provides novel processes for producing 2,5-furandicarboxylic acid (FDCA). In some embodiments, the processes disclosed herein provide beneficial and advantageously high yields of FDCA. In some embodiments, the processes disclosed herein provide beneficial and advantageous selectivity of FDCA that minimizes the production of side-products. For example, in some embodiments, the processes disclosed herein produce FDCA with minimal production of 2- furoic acid as a side product. In some embodiments, the processes disclosed herein use heterogeneous sugar derivative substrates to produce FDCA in high purity. In some embodiments, the processes disclosed herein produce FDCA in yields and purity sufficient for use in commercial production of commodity chemicals, such as the commercial production of polyesters, polyamides, and polyurethanes. .

[0100] In some embodiments provided herein, the present disclosure provides a process for producing FDCA, the process comprising contacting a sugar derivative substrate with a Bronsted acid and a halide salt in the presence of a water-miscible organic solvent to form a reaction mixture producing FDCA. In some embodiments, 2-furoic acid will be formed in the reaction mixture.

[0101] Without being limited by a particular theory, the conversion of a sugar derivative substrate comprising C₆-aldaric acids (including e.g., esters and salts of C₆-aldaric acids) to FDCA may occur via a Bronsted acid-catalyzed cyclodehydration of the C₆-aldaric acids to produce FDCA, as shown in Scheme 1. Also without being limited by a particular theory, mono- and di-lactones of C₆-aldaric acids may convert to the corresponding C₆- aldaric acids in acidic solution, as shown in Scheme 2, which can then be converted to FDCA according to the cyclodehydration process shown in Scheme 1. Additionally, without being limited by a particular theory, mono- and di-lactones of C₆-aldaric acids may be converted directly to FDCA. The conversion of sugar derivative substrates to FDCA in surprisingly high yield may be realized with various different halide salts and Bronsted acids, and may also be realized with various concentrations of halide salts and Bronsted acids.

Scheme 1: Cyclodehydration of Ce-aldaric acids to FDCA

Scheme 2: Equilibrium of mono-, di-lactones and Ce-aldaric acids

[0102] In some embodiments of the processes for forming FDCA disclosed herein, the sugar derivative substrate may be a homogenous sugar derivative substrate. In some embodiments the sugar derivative substrate may be a heterogenous sugar derivative substrate. In some embodiments, the sugar derivative substrate may be a C₆-aldaric acid, or a lactone, ester, or salt of a C₆-aldaric acid. In some embodiments, the sugar derivative substrate may be glucaric acid, or a lactone, ester, or salt of glucaric acid. In one embodiment, the sugar derivative substrate may be glucaric acid. In one embodiment, the sugar derivative substrate may be sodium glucarate. In one embodiment, the sugar derivative substrate may be potassium glucarate. In one embodiment, the sugar derivative substrate may be calcium glucarate. In one embodiment, the sugar derivative substrate may be glucaric acid 1,4-monolactone. In one embodiment, the sugar derivative substrate may be glucaric acid 3,6-monolactone. In one embodiment, the sugar derivative substrate may be glucaric acid dilactone. In one embodiment, the sugar derivative substrate may be galactaric (mucic) acid. In one embodiment, the sugar derivative substrate may be sodium galactarate. In one embodiment, the sugar derivative substrate may be potassium galactarate. In one embodiment, the sugar derivative substrate may be calcium galactarate. In one embodiment, the sugar derivative substrate may be galactaric acid 1,4-monolactone. In one embodiment, the sugar derivative substrate may be galactaric acid 3,6-monolactone. In one embodiment, the sugar derivative substrate may be mannaric acid. In one embodiment, the sugar derivative substrate may be sodium mannarate. In one embodiment, the sugar derivative substrate may be potassium mannarate. In one embodiment, the sugar derivative substrate may be calcium mannarate. In one embodiment, the sugar derivative substrate may be mannaric acid 1,4-monolactone. In one embodiment, the sugar derivative substrate may be mannaric acid 3,6-monolactone. In one embodiment, the sugar derivative substrate may be mannaric acid dilactone. In one embodiment, the sugar derivative substrate may comprise a mixture of two or more of any of the aforementioned sugar derivative substrates.

[0103] When carrying out a process of the present disclosure, the sugar derivative substrate may be present in the reaction at any concentration up to its solubility limit. In some embodiments, the concentration of sugar derivative substrate in the reaction mixture may be e.g., at least 0.01 M, at least 0.02 M, at least 0.05 M, at least 0.10 M, at least 0.15 M, at least 0.25 M, at least 0.30 M, at least 0.35 M, at least 0.40 M, at least 0.45 M, at least 0.50 M, at least 0.55 M, at least 0.60 M, at least 0.70 M, at least 0.80 M, at least 0.90 M, at least 1.0 M, at least 2.0 M, at least 3.0 M, at least 4.0 M, at least 5.0 M, at least 6.0 M, at least 7.0 M, at least 8.0 M, at least 9.0 M, or at least 10.0 M or may be within a range defined by any two of the aforementioned concentrations. In some embodiments, the concentration of sugar derivative substrate in the reaction mixture ranges from e.g., 0.01-10.0 M, 0.02-5.0 M, 0.05- 2.0 M, 0.10-1.0 M, 0.15-1.0 M, 0.20-1.0 M, 0.2-1.25 M, 0.4-1.25 M, 0.5-1.0 M, or 0.6-1.25 M, or may be within a range defined by any of two of the aforementioned concentrations. The sugar derivative substrate may be present in the reaction mixture at a concentration of at least 0.20 M. The sugar derivative substrate may be present in the reaction mixture at a concentration of e.g., at least 0.2 M, or at least 0.3 M, or at least 0.4 M, or at least 0.5 M, or at least 0.6 M, or at least 0.8 M, or at least 1.0 M, or at least 1.25 M, or at least 1.5 M or may be within a range defined by any two of the aforementioned concentrations. In some embodiments, the sugar derivative substrate may be present in the reaction mixture at in a concentration that ranges from between e.g., 0.2-2.0 M, 0.3-1.5 M, 0.4-1.25 M, 0.5-1.25 M, or 0.6-1.0 M, or may be within a range defined by any of two of the aforementioned concentrations.

[0104] Water-miscible organic solvents are suitable for use in the practice of the present disclosure. Without wishing to be bound by any particular theory, the water-miscible organic solvent is believed to facilitate the efficient conversion of the sugar derivative substrate to FDCA by both solubilizing the sugar derivative substrate and, at least to some extent, the Bronsted acid and halide salt. In one embodiment, the water-miscible organic solvent includes but is not limited to 1,4-dioxane, tetrahydrofuran (THF), sulfolane, dimethylfoimamide (DMF), dimethylsulfoxide (DMSO), methyl ethyl ketone, acetic acid, ethanol, «-propanol, 1,3 -propanediol, isopropanol, «-butanol, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, acetonitrile, ethylene glycol, propylene glycol, pyridine, and/or a glyme. In one embodiment, the water-miscible organic solvent may comprise or consist of 1,4-dioxane. In one embodiment, the water-miscible organic solvent may comprise or consist of tetrahydrofuran (THF). In one embodiment, the water-miscible organic solvent may comprise or consist of sulfolane. In one embodiment, the water- miscible organic solvent may comprise or consist of N-methyl-2-pyrrolidinone (NMP). In one embodiment, the water-miscible organic solvent does not comprise NMP. In one embodiment, the water-miscible organic solvent may comprise or consist of dimethylfoimamide (DMF). In one embodiment, the water-miscible organic solvent may comprise or consist of dimethylsulfoxide (DMSO). In one embodiment, the water-miscible organic solvent may comprise or consist of methyl ethyl ketone. In one embodiment, the water-miscible organic solvent may comprise or consist of acetic acid. In one embodiment, the water-miscible organic solvent may comprise or consist of ethanol. In one embodiment, the water-miscible organic solvent may comprise or consist of «-propanol. In one embodiment, the water-miscible organic solvent may comprise or consist of 1,3-propanediol. In one embodiment, the water-miscible organic solvent may comprise or consist of isopropanol. In one embodiment, the water-miscible organic solvent may comprise or consist of «-butanol. In one embodiment, the water-miscible organic solvent may comprise or consist of 1,2-butanediol. In one embodiment, the water-miscible organic solvent may comprise or consist of 1,3-butanediol. In one embodiment, the water-miscible organic solvent may comprise or consist of 1,4-butanediol. In one embodiment, the water-miscible organic solvent may comprise or consist of 1,5-pentanediol. In one embodiment, the water- miscible organic solvent may comprise or consist of acetonitrile. In one embodiment, the water-miscible organic solvent may comprise or consist of ethylene glycol. In one embodiment, the water-miscible organic solvent may comprise or consist of propylene glycol. In one embodiment, the water-miscible organic solvent may comprise or consist of pyridine. In some embodiments, the water-miscible organic solvent may comprise or consist of a glyme. In one embodiment, the glyme may comprise or consist of 1,2-dimethoxyethane. In one embodiment, the glyme may comprise or consist of ethyl glyme. In one embodiment, the glyme may comprise or consist of diethylene glycol dimethyl ether. In one embodiment, the glyme may comprise or consist of ethyl diglyme. In one embodiment, the glyme may comprise or consist of triglyme. In one embodiment, the glyme may comprise or consist of butyldiglyme. In one embodiment, the glyme may comprise or consist of tetraglyme. In one embodiment, the glyme may comprise or consist of a polyglyme. In some embodiments, the processes of the present disclosure may utilize a mixture comprising two or more of any of the aforementioned water-miscible organic solvents.

[0105] The processes of the present disclosure may be carried out using a variety of Bronsted acids. In one embodiment, the Bronsted acid may comprise or consist of hydrochloric acid. In one embodiment, the Bronsted acid may comprise or consist of hydrobromic acid. In one embodiment, the Bronsted acid may comprise or consist of hydroiodic acid. In one embodiment, the Bronsted acid may comprise or consist of sulfuric acid. In one embodiment, the Bronsted acid may comprise or consist of nitric acid. In one embodiment, the Bronsted acid may comprise or consist of phosphoric acid. In one embodiment, the Bronsted acid may comprise or consist of acetic acid. In one embodiment, the Bronsted acid may comprise or consist of trifluoracetic acid. In one embodiment, the Bronsted acid may comprise or consist of formic acid. In one embodiment, the Bronsted acid may comprise or consist of methanesulfonic acid (MsOH). In one embodiment, the Bronsted acid may comprise or consist of p-toluenesulfonic acid (p-TsOH). In one embodiment, the Bronsted acid may comprise or consist of benzenesulfonic acid. In one embodiment, the Bronsted acid may comprise or consist of trifluoromethanesulfonic acid (TfOH). In some embodiments, the processes of the present disclosure may be carried out utilizing a combination of two or more of the aforementioned Bronsted acids.

[0106] When carrying out the processes of the present disclosure, the Bronsted acid may be present in the reaction at any concentration up to its solubility limit. In some embodiments, the concentration of Bronsted acid in the reaction mixture may be at least e.g., 0.1 M, at least 0.2 M, at least 0.3 M, at least 0.4 M, at least 0.5 M, at least 0.6 M, at least 0.7 M, at least 0.8 M, at least 0.9 M, at least 1.0 M, at least 2.0 M, at least 3.0 M, at least 4.0 M, at least 5.0 M, at least 6.0 M, at least 7.0 M, at least 8.0 M, at least 9.0 M, or at least 10.0 M or a concentration that is within a range defined by any two of the aforementioned concentrations. In some embodiments, the concentration of Bronsted acid in the reaction mixture ranges from e.g., 0.1-10.0 M, 0.5-5.0 M, 1.0-4.0 M, or 2.0-3.0 M, or may be within a range defined by any of two of the aforementioned concentrations. The Bronsted acid may be present in the reaction mixture at a concentration of e.g., at least 0.50 M. The Bronsted acid may be present in the reaction mixture at a concentration of e.g., at least 0.5 M, or at least 1.0 M, or at least 1.5 M, or at least 2.0 M, or at least 3.0 M, or at least 3.5 M, or at least 4.0 M, or at least 4.5 M, or at least 5.0 M, or at least 4.5 M, or at least 5.0 M, or at least 4.5 M, or at least 5.0 M, or at least 4.5 M, or at least 5.0 M, or at least 4.5 M, or at least 5.0 M, or at least 4.5 M, or at least 5.0 M, or at least 4.5 M, or at least 5.0 M, or at least 5.5 M, or at least 6.0 M, or at least 6.5 M, or at least 7.0 M, or at least 7.5 M, or at least 8.0 M, or at least 8.5 M, or at least 9.0 M, or at least 9.5 M, or at least 10.0 M or a concentration that is within a range defined by any two of the aforementioned concentrations. In some embodiments, the Bronsted acid may be present in the reaction mixture at a concentration that ranges from between 0.5-10.0 M, 1.0-5.0 M, 1.5-4.0 M, 2.0-4.0 M, or 2.0-6.0 M, or may be within a range defined by any of two of the aforementioned concentrations. [0107] The processes of the present disclosure may be carried out using a variety of halide salts. In some embodiments, the halide salt may comprise or consist of a metal halide salt. In one embodiment, the metal halide salt may comprise or consist of LiCl. In one embodiment, the metal halide salt may comprise or consist of LiBr. In one embodiment, the metal halide salt may comprise or consist of Lil. In one embodiment, the metal halide salt may comprise or consist of NaCl. In one embodiment, the metal halide salt may comprise or consist of NaBr. In one embodiment, the metal halide salt may comprise or consist of Nal. In one embodiment, the metal halide salt may comprise or consist of KF. In one embodiment, the metal halide salt may comprise or consist of KC1. In one embodiment, the metal halide salt may comprise or consist of KBr. In one embodiment, the metal halide salt may comprise or consist of KI. In one embodiment, the metal halide salt may comprise or consist of CaCl₂. In one embodiment, the metal halide salt may comprise or consist of CaBr₂. In one embodiment, the metal halide salt may comprise or consist of MgCl₂. In one embodiment, the metal halide salt may comprise or consist of MgBr₂. In one embodiment, the metal halide salt may comprise or consist of CuCl. In one embodiment, the metal halide salt may comprise or consist of CuCl₂. In one embodiment, the metal halide salt may comprise or consist of CuBr. In one embodiment, the metal halide salt may comprise or consist of CuBr₂. In one embodiment, the metal halide salt may comprise or consist of FeCl₂. In one embodiment, the metal halide salt may comprise or consist of FeCl₃. In one embodiment, the metal halide salt may comprise or consist of FeBr₂. In one embodiment, the metal halide salt may comprise or consist of FeBr₃. In one embodiment, the metal halide salt may comprise or consist of ZnCl₂. In one embodiment, the metal halide salt may comprise or consist of ZnBr₂. In one embodiment, the metal halide salt may comprise or consist of NiCl₂. In one embodiment, the metal halide salt may comprise or consist of NiBr₂. In some embodiments, the halide salt may comprise or consist of a tetraalkylammonium halide salt. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetramethylammonium choride. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetramethylammonium bromide. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetramethylammonium iodide. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetraethylammonium chloride. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetraethylammonium bromide. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetraethylammonium iodide. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetrabutylammonium chloride. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetrabutylammonium bromide. In one embodiment, the tetraalkylammonium salt may comprise or consist of tetrabutylammonium iodide. In some embodiments, the processes of the present disclosure may utilize hydrates of any of the aforementioned halide salts. In some embodiments, the processes of the present disclosure may utilize two or more of any of the aforementioned halide salts.

[0108] When carrying out the processes of the present disclosure, the halide salt may be present in the reaction at any concentration up to its solubility limit. In some embodiments, the concentration of halide salt in the reaction mixture may be e.g., at least 0.01 M, at least 0.02 M, at least 0.05 M, at least 0.10 M, at least 0.15 M, at least 0.25 M, at least 0.30 M, at least 0.35 M, at least 0.40 M, at least 0.45 M, at least 0.50 M, at least 0.60 M, at least 0.70 M, at least 0.80 M, at least 0.90 M, at least 1.0 M, at least 1.2 M, at least 1.5 M, at least 2.0 M, at least 2.5 M, or at least 3.0 M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the concentration of halide salt in the reaction mixture ranges from e.g., 0.01-3.0 M, 0.05-2.0 M, 0.10-1.0 M, or 0.20-0.50 M, or may be within a range defined by any of two of the aforementioned concentrations. The halide salt may be present in the reaction mixture at a concentration of e.g., at least 0.20 M. The halide salt may be present in the reaction mixture at a concentration of e.g., at least 0.2 M, or at least 0.3 M, or at least 0.4 M, or at least 0.5 M, or at least 0.6 M, or at least 0.8 M, or at least 1.0M, or at least 1.2 M, or at least 1.25 M, or at least 1.5 M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the halide salt may be present in the reaction mixture at a concentration that ranges from e.g., between 0.2-2.0 M, 0.3-1.5 M, 0.4-1.2 M, 0.4-1.25 M, 0.5-1.25 M, or 0.6-1.0 M, or may be within a range defined by any of two of the aforementioned concentrations. In some embodiments, the halide salt may be present in the reaction mixture at a concentration of at least 0.1 M. In some embodiments, the halide slat may be present in the reaction mixture at a concentration of less than 2.0 M, or less than 1.5 M, or less than 1.3 M, or less than 1 M, or less than 0.75 M, or less than 0.5 M but not zero. [0109] The processes of the present disclosure may be particularly sensitive to both the concentration of halide salt present and to the molar ratio of sugar derivative substrate to the halide salt. For example, in some embodiments, the molar ratio of sugar derivative substrate to halide salt may be present in the reaction mixture in a molar ratio of e.g., 5:1 to 1:5, for example 4.5:1 or 4:1 or 3.5:1 or 3:1 or 2.75:1 or 2.5:1 or 2:1 or 1:75:1 or 1.5:1 or 1.25:1 or 1:1 or 1:1.25 or 1:1.5 or 1:1.75 or 1:2 or 1:2.25 or 1:2.5 or 1:2.75 or 1:3 or 1:3.5 or 1:4 or 1:4.5, or within any range defined by any two of the aforementioned molar ratios.

[0110] In the processes of the present disclosure, it may be desirable to select a particular combination of Bronsted acid and halide salt. For example, particular salts may be desired when hydrochloric acid may be chosen as the Bronsted acid. In some embodiments provided herein, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of LiCl. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of LiBr. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of NaCl. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of Nal. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of KC1. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of KBr. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of KI. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of CaCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of CaBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of MgCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of MgBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of CuCl. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of CuCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of CuBr. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of CuBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of FeCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of FeCl₃. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of FeBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of FeBr₃. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of ZnCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of NiCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of NiBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetramethylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetramethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetramethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetraethylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetraethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetraethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetrabutylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetrabutylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of hydrochloric acid and the halide salt may comprise or consist of tetrabutylammonium iodide.

[0111] In the processes of the present disclosure, it may be desirable to select a particular halide salt when other Bronsted acid(s) are chosen for the cyclization and dehydration of the sugar derivative substrate. In some embodiments provided herein, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of LiCl. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of LiBr. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of NaCl. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of Nal. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of KC1. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of KBr. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of KI. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of CaCl₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of CaBr₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of MgCl₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of MgBr₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of CuCl. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of CuCl₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of CuBr. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of CuBr₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of FeCl₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of FeCl₃. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of FeBr₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of FeBr₃. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of ZnCl₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of NiCl₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of NiBr₂. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetramethylammonium choride. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetramethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetramethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetraethylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetraethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetraethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetrabutylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetrabutylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of methanesulfonic acid and the halide salt may comprise or consist of tetrabutylammonium iodide.

[0112] In some embodiments provided herein, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of LiCl. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of LiBr. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of NaCl. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of Nal. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of KC1. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of KBr. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of KI. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of CaCl₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of CaBr₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of MgCl₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of MgBr₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of CuCl. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of CuCl₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of CuBr. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of CuBr₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of FeCl₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of FeCl₃. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of FeBr₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of FeBr₃. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of ZnCl₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of NiCl₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of NiBr₂. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetramethylammonium choride. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetramethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetramethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetraethylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetraethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetraethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetrabutylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetrabutylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of sulfuric acid and the halide salt may comprise or consist of tetrabutylammonium iodide.

[0113] In some embodiments provided herein, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of LiCl. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of LiBr. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of NaCl. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of Nal. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of KC1. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of KBr. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of KI. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of CaCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of CaBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of MgCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of MgBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of CuCl. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of CuCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of CuBr. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of CuBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of FeCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of FeCl₃. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of FeBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of FeBr₃. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of ZnCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of NiCl₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of NiBr₂. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetramethylammonium choride. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetramethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetramethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetraethylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetraethylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetraethylammonium iodide. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetrabutylammonium chloride. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetrabutylammonium bromide. In some embodiments, the Bronsted acid may comprise or consist of hydrobromic acid and the halide salt may comprise or consist of tetrabutylammonium iodide.

[0114] The processes of the present carrying out the processes of the present disclosure, it may be desirable to carry out the reaction with a particular molar ratio of Bronsted acid to halide salt in the reaction mixture. In some embodiments, the molar ratio of Bronsted acid to halide salt may be in the range of e.g., 20:1 to 1:20, for example 20:1, 19:1, 18:1, 17:1, 16:1, 15:1, 14:1, 13:1, 12:1, 11:1, 10:1, 9:1, 8:1, 7:1, 6:1, 5:1, 4:1, 3:1, 2:1, 1:1, 1:2, 1:3, 1:4, 1:5, 1:6, 1:7, 1:8, 1:9, 1:10, 1:11, 1:12, 1:13, 1:14, 1:15, 1:16, 1:17, 1:18, 1:19, or 1:20, or within any range defined by any two of the aforementioned molar ratios. In some embodiments, the molar ratio of Bronsted acid to halide salt may be 20:1. In some embodiments, the molar ratio of Bronsted acid to halide salt may be 17.5:1. In some embodiments, the molar ratio of Bronsted acid to halide salt may be 14:1. In some embodiments, the molar ratio of Bronsted acid to halide salt may be 9:1. For example, in some embodiments, hydrochloric acid and ZnCl₂ may be present in the reaction mixture in a molar ratio ranging from e.g., 5:1 to 20:1, or 8:1 to 18:1, or 10:1 to 15:1, or within any range defined by any two of the aforementioned molar ratios. In some embodiments, the molar ratio of methanesulfonic acid to CaBr₂ may be present in the reaction mixture in a molar ratio of 3:1 to 1:3, for example 2.75:1 or 2.5:1 or 2:1 or 1:75:1 or 1.5:1 or 1.25:1 or 1:1 or 1:1.25 or 1:1.5 or 1:1.75 or 1:2 or 1:2.25 or 1:2.5 or 1:2.75, or within any range defined by any two of the aforementioned molar ratios. In some embodiments, the molar ratio of methanesulfonic acid to LiBr may be present in the reaction mixture in a molar ratio of 3:1 to 1:3, for example 2.75:1 or 2.5:1 or 2:1 or 1:75:1 or 1.5:1 or 1.25:1 or 1:1 or 1:1.25 or 1:1.5 or 1:1.75 or 1:2 or 1:2.25 or 1:2.5 or 1:2.75, or within any range defined by any two of the aforementioned molar ratios.

[0115] Particular combinations of Bronsted acid and halide salt may be desired in connection with using a specific solvent. For example, in some embodiments where the water-miscible organic solvent comprises or consists of 1,4-dioxane, the Bronsted acid comprises or consists of HC1, and the halide salt comprises or consists of ZnCl₂. In some embodiments, water-miscible organic solvent comprises or consists of 1,4-dioxane, the Bronsted acid comprises or consists of HC1, and the halide salt comprises or consists of ZnBr₂. In some embodiments, water-miscible organic solvent comprises or consists of 1,4- dioxane, the Bronsted acid comprises or consists of HC1, and the halide salt comprises or consists of CaBr₂. In some embodiments, water-miscible organic solvent comprises or consists of 1,4-dioxane, the Bronsted acid comprises or consists of HC1, and the halide salt comprises or consists of NaBr.

[0116] In some embodiments, the water-miscible organic solvent comprises or consists of sulfolane, the Bronsted acid comprises or consists of MsOH, and the halide salt comprises or consists of LiBr. In some embodiments, the water-miscible organic solvent comprises or consists of sulfolane, the Bronsted acid comprises or consists of MsOH, and the halide salt comprises or consists of CaBr₂. In some embodiments, the water-miscible organic solvent comprises or consists of sulfolane, the Bronsted acid comprises or consists of HC1, and the halide salt comprises or consists of CaBr₂. In some embodiments, the water-miscible organic solvent comprises or consists of sulfolane, the Bronsted acid comprises or consists of H₂S0₄, and the halide salt comprises or consists of CaBr₂. In some embodiments, the water- miscible organic solvent comprises or consists of sulfolane, the Bronsted acid comprises or consists of HBr, and the halide salt comprises or consists of LiBr.

[0117] The processes of the present disclosure may be carried out by optionally including water in the reaction mixture. In some embodiments, the amount of water included in the reaction mixture is the residual amount of water present in the water-miscible organic solvent. In some embodiments, water may be added to the reaction mixture. In some embodiments, the concentration of water in the reaction mixture may be e.g., at least 0.01 M, at least 0.02 M, at least 0.05 M, at least 0.10 M, at least 0.15 M, at least 0.25 M, at least 0.30 M, at least 0.35 M, at least 0.40 M, at least 0.45 M, at least 0.50 M, at least 0.60 M, at least 0.70 M, at least 0.80 M, at least 0.90 M, at least 1.0 M, at least 1.5 M, at least 2.0 M, at least 2.5 M, or at least 3.0 M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the concentration of water in the reaction mixture ranges from e.g., 0.01-3.0 M, 0.05-2.0 M, 0.10-1.0 M, or 0.20-0.50 M, or may be within a range defined by any of two of the aforementioned concentrations. The water may be present in the reaction mixture at a concentration of at least 0.20 M. The water may be present in the reaction mixture at a concentration of e.g., at least 0.2 M, or at least 0.3 M, or at least 0.4 M, or at least 0.5 M, or at least 0.6 M, or at least 0.8 M, or at least 1.0M, or at least 1.25 M, or at least 1.5 M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the water may be present in the reaction mixture at a concentration that ranges from e.g., between 0.2-2.0 M, 0.3-1.5 M, 0.4-1.25 M, 0.5-1.25 M, or 0.6-1.0 M, or may be within a range defined by any of two of the aforementioned concentrations.

[0118] In some embodiments, the processes of the present disclosure may be carried out by optionally including water in the reaction mixture. In some embodiments, the amount of water included in the reaction mixture is the residual amount of water present in the water-miscible organic solvent. In some embodiments, water may be added to the reaction mixture. In some embodiments, the concentration of water in the reaction mixture may be e.g., at least 0.01 M, at least 0.02 M, at least 0.05 M, at least 0.10 M, at least 0.15 M, at least 0.24 M, at least 0.25 M, at least 0.30 M, at least 0.35 M, at least 0.40 M, at least 0.45 M, at least 0.50 M, at least 0.60 M, at least 0.70 M, at least 0.80 M, at least 0.90 M, at least 1.0 M, at least 1.5 M, at least 2.0 M, at least 2.5 M, at least 3.0 M, at least 3.5 M, at least 4.0 M, at least 4.5 M, at least 5.0 M, at least 6.0 M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the concentration of water in the reaction mixture ranges from e.g., 0.01-6.0 M, 0.02-5.0 M, 0.03-3.0 M, 0.05-2.0 M, 0.10-1.0 M, or 0.20-0.50 M, or may be within a range defined by any of two of the aforementioned concentrations. The water may be present in the reaction mixture at a concentration of at least 0.20 M. The water may be present in the reaction mixture at a concentration of e.g., at least 0.2 M, or at least 0.3 M, or at least 0.4 M, or at least 0.5 M, or at least 0.6 M, or at least 0.8 M, or at least 1.0M, or at least 1.25 M, or at least 1.5 M, or at least 3.0 M, or at least 5.0 M, or at least 6.0 M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the water may be present in the reaction mixture at a concentration that ranges from e.g., between 0.2-5.0 M, 0.3-2.0 M, 0.4-1.5 M, 0.5-1.25 M, 0.6-1.25 M, or 0.8-1.0 M, or may be within a range defined by any of two of the aforementioned concentrations. [0119] The processes of the present disclosure may be carried out by optionally including an alcohol in the reaction mixture. In one embodiment, the alcohol may comprise or consist of methanol. In one embodiment, the alcohol may comprise or consist of ethanol. In one embodiment, the alcohol may comprise or consist of n-propanol. In one embodiment, the alcohol may comprise or consist of isopropanol. In one embodiment, the alcohol may comprise or consist of n-butanol. In one embodiment, the alcohol may comprise or consist of 2-(2-chloroethoxy)ethan-l-ol (CEE). In some embodiments, the processes of the present disclosure may utilize two or more of any of the aforementioned alcohols. In some embodiments, the concentration of alcohol in the reaction mixture may be e.g., at least 0.01 M, at least 0.02 M, at least 0.05 M, at least 0.10 M, at least 0.15 M, at least 0.25 M, at least 0.30 M, at least 0.35 M, at least 0.40 M, at least 0.45 M, at least 0.50 M, at least 0.60 M, at least 0.70 M, at least 0.80 M, at least 0.90 M, or at least 1.0 M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the concentration of water in the reaction mixture ranges from e.g., 0.01-1.0 M, 0.02-1.0 M, 0.05-1.0 M, 0.10- 1.0M, or 0.10-0.50 M, or may be within a range defined by any of two of the aforementioned concentrations. The alcohol may be present in the reaction mixture at a concentration of at least 0.02 M. Typically, the alcohol may be present in the reaction mixture at a concentration of e.g., at least 0.1 M, or at least 0.2 M, or at least 0.3 M, or at least 0.4 M, or at least 0.5 M, or at least 0.6 M, or at least 0.8 M, or at least 1.0M or within a range defined by any two of the aforementioned concentrations. In some embodiments, the alcohol may be present in the reaction mixture at in a concentration that ranges from e.g., between 0.1-1.0 M, 0.2-0.6 M, or 0.3-0.5 M, or may be within a range defined by any of two of the aforementioned concentrations.

[0120] The dehydration of the sugar derivative substrate is typically carried out at an elevated temperature. Typically, the dehydration is carried out at a temperature in the range from or any number in between e.g., 60°C to 200°C, such as e.g., 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 180, 190, or 200 °C or within a range defined by any two of the aforementioned temperatures. Often, the dehydration of the sugar derivative substrate is carried out at a temperature in the range from or any number in between e.g., 60°C to 180°C, or in the range from or any number in between 70°C to 160°C such as e.g., 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 170, or 180 °C or within a range defined by any two of the aforementioned temperatures.

[0121] The dehydration of the sugar derivative substrate may be carried out while pressuring the reaction mixture. For example, in some embodiments, the dehydration of the sugar derivative substrate may be performed in a vessel pressurized with a gas. In some embodiments, the gas comprises or consists of nitrogen. In some embodiments, the gas comprises or consists of argon. In some embodiments, the gas comprises or consists of helium. In some embodiments, the gas comprises or consists of carbon dioxide. Typically, the reaction mixture will be pressurized to a pressure ranging from or any number in between e.g., 15-500 psi. In some embodiments, the reaction mixture is pressurized to a pressure in the range from or any number in between e.g., 15-500 psi, 25-400 psi, 50-400 psi, 100-300 psi, 150-250 psi, or 250-350 psi, or within a range defined by any two of the aforementioned pressures.

[0122] The dehydration of the sugar derivative substrate is typically carried out for a time period ranging from or any time frame in between 1 h to 7 days. Typically, the dehydration of the sugar derivative is carried out for a time in the range of e.g., 1 h and 96 h or any number in between 1 h to 96 h, such as e.g., 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 28, 32, 36, 40, 44, 48, 52, 56, 60, 64, 68, 72, 76, 80, 84, 88, 92 or 96 h, or within a range defined by any two of the aforementioned times.

[0123] In some embodiments, the dehydration of the sugar derivative substrate is typically carried out for a time period ranging from or any time frame in between 0.5 h to 7 days. Typically, the dehydration of the sugar derivative is carried out for a time in the range of e.g., 0.5 h and 96 h or any number in between 0.5 h to 96 h, such as e.g., 0.5, 1, 2, 3, 4, 5,

6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 28, 32, 36, 40, 44, 48, 52, 56, 60, 64, 68, 72, 76, 80, 84, 88, 92 or 96 h, or within a range defined by any two of the aforementioned times.

[0124] In some embodiments, the dehydration of the sugar derivative substrate is typically carried out for a time period ranging from or any time frame in between 1 min to 7 days. Typically, the dehydration of the sugar derivative is carried out for a time in the range of e.g., 1 min and 24 h or any number in between 1 min and 24 h, such as e.g., 1, 2, 3, 4, 5, 6,

7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 28, 32, 36, 40, 44, 48, 52, 56 or 60 min, or 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23 or 24 h, or within a range defined by any two of the aforementioned times.

[0125] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate comprising or consisting of a substrate selected from the group of glucaric acid dilactone, glucaric acid 1,4-monolactone, and/or potassium glucarate; a Bronsted acid selected from the group of HC1, HBr, MsOH, and/or H₂S0₄; a halide salt selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water-miscible organic solvent that comprises or consists of sulfolane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-2.5 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C or 110-160 °C. In some embodiments, the temperature of the reaction mixture may be 130-160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3- 24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130- 160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0126] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture including a sugar derivative substrate at a molar concentration in the range from or any number in between 0.1-3.5 M and the sugar derivative substrate comprises or consists of a substrate selected from the group of glucaric acid dilactone, glucaric acid 1,4-monolactone, and/or potassium glucarate; a Bronsted acid at a molar concentration in the range of from or any number in between 0.2-3.6 M and the Bronstead acid is selected from the group of HC1, HBr, MsOH, and/or H₂S0₄; a halide salt at a molar concentration in the range of from or any number in between 0.1-3 M and the halide salt is selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water- miscible organic solvent that comprises or consists of sulfolane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-2.5 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3- 24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130- 160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0127] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate comprising or consisting of a substrate selected from the group of glucaric acid dilactone, glucaric acid 1,4-monolactone, and/or potassium glucarate; a Bronsted acid selected from the group of HC1, HBr, MsOH, and/or H₂S0₄; a halide salt selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water-miscible organic solvent that comprises or consists of sulfolane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-6.0 M. In some embodiments, the water-miscible organic solvent may comprise water at a concentration at 5.0 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-150 °C. In some embodiments, the temperature of the reaction mixture may be 140 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 0.5-24 h. In some embodiments, the reaction may proceed for a time of 1 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0128] In some embodiments, the process for producing FDCA may comprise a reaction mixture comprising or consisting of a sugar derivative substrate comprising or consisting of glucaric acid dilactone; a Bronsted acid selected from the group of HC1 and/or MsOH; a halide salt selected from the group of ZnCl₂, LiBr, and/or CaBr₂; and a water- miscible organic solvent that comprises sulfolane. The water-miscible organic solvent may comprise water. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3-24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0129] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate at a molar concentration in the range from or any number in between 1-3.5 M and the sugar derivative substrate comprises or consists of glucaric acid dilactone; a Bronsted acid at a molar concentration in the range of from or any number in between 0.2-1.6 M and the Bronstead acid is selected from the group of HC1 and/or MsOH; a halide salt at a molar concentration of approximately 2 M and the halide salt is selected from the group of ZnCl₂, LiBr, and/or CaBr₂; and a water-miscible organic solvent that comprises or consists of sulfolane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0.2-0.4 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3-24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0130] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate that comprises or consists of a substrate selected from the group of glucaric acid dilactone, glucaric acid 1,4-monolactone, and/or potassium glucarate; a Bronsted acid selected from the group of HC1 and/or HBr; a halide salt selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water-miscible organic solvent that comprises or consists of 1,4- dioxane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-2.5 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3-24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0131] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate at a molar concentration in the range from or any number in between 0.1-3.5 M and the sugar derivative substrate comprises or consists of a substrate selected from the group of glucaric acid dilactone, glucaric acid 1,4-monolactone, and/or potassium glucarate; a Bronsted acid at a molar concentration in the range of from or any number in between 0.2-3.6 M and the Bronstead acid is selected from the group of HC1 and/or HBr; a halide salt at a molar concentration in the range of from or any number in between 0.1-3 M and the halide salt is selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water- miscible organic solvent that comprises or consists of 1,4-dioxane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-2.5 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3-24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0132] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate comprising or consisting of glucaric acid dilactone; a Bronsted acid comprising or consisting of HC1; a halide salt selected from the group of ZnCl₂, LiBr, and/or CaBr₂; and a water- miscible organic solvent that comprises or consists of 1,4-dioxane. The water-miscible organic solvent may comprise or consist of water. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3-24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0133] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate at a molar concentration in the range from or any number in between 1-3.5 M and the sugar derivative substrate comprises or consists of glucaric acid dilactone; a Bronsted acid at a molar concentration in the range of from or any number in between 0.2-1.6 M and the Bronstead acid comprises or consists of HC1; a halide salt at a molar concentration of approximately 2 M and the halide salt is selected from the group of ZnCl₂, LiBr, and/or CaBr₂; and a water-miscible organic solvent that comprises or consists of 1,4-dioxane. The water-miscible organic solvent may comprise or consist of water at a concentration ranging from or any number in between 0.2-0.4 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3-24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0134] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate comprising or consisting of a substrate selected from the group of mannaric acid, mannaric acid dilactone, mannaric acid 1,4-monolactone, sodium mannarate, and/or potassium glucarate; a Bronsted acid selected from the group of HC1, HBr, MsOH, and/or H₂S0₄; a halide salt selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water-miscible organic solvent that comprises or consists of sulfolane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-2.5 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3-24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0135] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate, preferably a heterogeneous sugar derivative substrate, comprising or consisting of a substrate selected from the group of mannaric acid dilactone, glucaric acid dilactone, and/or galactaric acid; a Bronsted acid selected from the group of HC1, HBr, MsOH, and/or H₂S0₄; a halide salt selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water- miscible organic solvent that comprises or consists of sulfolane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-2.5 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-120 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 3- 24 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130- 160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0136] In some embodiments, the process for producing FDCA may comprise or consist of a reaction mixture comprising or consisting of a sugar derivative substrate, preferably a heterogeneous sugar derivative substrate, comprising or consisting of a substrate selected from the group of mannaric acid dilactone, glucaric acid dilactone, and/or galactaric acid; a Bronsted acid selected from the group of HC1, HBr, MsOH, and/or H₂S0₄; a halide salt selected from the group of ZnBr₂, ZnCl₂, NaBr, LiBr, MgBr₂, and/or CaBr₂; and a water- miscible organic solvent that comprises or consists of sulfolane. The water-miscible organic solvent may comprise water at a concentration ranging from or any number in between 0-6.0 M. In some embodiments, the water-miscible organic solvent may comprise water at a concentration of 5.0 M. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-150 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 90-200 °C. In some embodiments, the temperature of the reaction mixture may range from or any number in between 110-180 °C. In some embodiments, the temperature of the reaction mixture may be 160 °C. In some embodiments, the temperature of the reaction mixture may be 140 °C. In some embodiments, the reaction may proceed for a time ranging from or any number in between 0.5-24 h. In some embodiments, the reaction may proceed for a time of 1 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 3 h. In some embodiments, the reaction may proceed for a time ranging from or any number in between 1 min to 24 h. In some embodiments, the reaction mixture is heated to a temperature of 90-200 °C, 110-160 °C, or 110-180 °C, preferably 130-160 °C, for time period of 1 min. to 24 hours, 1 min. to 3 hours, or 1 min. to 0.5 hours, preferably 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

[0137] The yield of FDCA produced from the sugar derivative substrate in accordance with one or more of the processes described herein can be e.g., at least 60%, or at least 70%, or at least 80%, or at least 90% or at least 95%, or at least 98% or at least 99%. In some embodiments, the yield ranges from between 85-90%, 87-92%, 90-95%, 92-97%, 95- 98%, or 97-99%, or is within a range defined by any of two of the aforementioned percentages.

[0138] In some embodiments, the FDCA produced from the sugar derivative substrate comprises or consists of e.g., from or any number in between 90 % to 99 % of FDCA by molar purity. In some embodiments, the molar purity of FDCA produced from the sugar derivative substrate can be at least 60%, or at least 70%, or at least 80%, or at least 90% or at least 95%, or at least 98% or at least 99% or within a range defined by any two of the aforementioned amounts. In some embodiments, the molar purity of FDCA produced from the sugar derivative substrate ranges from e.g., between 85-90%, 87-92%, 90-95%, 92- 97%, 95-98%, or 97-99%, or is within a range defined by any of two of the aforementioned percentages.

[0139] In some embodiments, one or more of the processes for producing FDCA described herein may generate an amount of 2-furoic acid impurities in the FDCA product. In some embodiments, the amount of 2-furoic acid present in the FDCA product comprises less than about 5% 2-furoic acid by weight percent, or less than about 2% 2-furoic acid by weight percent, or less than about 1% 2-furoic acid by weight percent, or less than about 0.5% 2- furoic acid by weight percent. In certain embodiments, the amount of 2-furoic acid present in the FDCA product comprises from or any number in between 0.05% to 5% 2- furoic acid by weight percent. In other embodiments, the amount of 2-furoic acid present in the FDCA product comprises from or any number in between 0.1% to 1% 2-furoic acid by weight percent. In still other embodiments, the amount of 2-furoic acid present in the FDCA product comprises from or any number in between 0.05 % to 0.5 % 2-furoic acid by weight percent. In some embodiments, the amount of 2-furoic acid present in the FDCA product comprises from or any number in between 0.5% to 1% 2-furoic acid by weight percent. In some embodiments, the amount of 2-furoic acid present in the FDCA product comprises from or any number in between 1% to 5% 2-furoic acid by weight percent.

[0140] In some embodiments, one or more of the processes for producing FDCA described herein may generate impurities in the FDCA product. In some embodiments, the impurityies may comprise 2-furoic acid. In some embodiments, the one or more processes produce FDCA and additional impurities, wherein the amount of FDCA relative to the additional impurities is at least 60%, or at least 65%, or at least 70%, or at least 75%, or at least 80%, or at least 85%, or at least 90%, or at least 91%, or at least 92%, or at least 93%, or at least 94%, or at least 95%, or at least 96%, or at least 97%, or at least 98%, or at least 99% by weight percent, or within any range defined by the aforementioned weight percents.

[0141] In some embodiments, one or more of the processes for producing FDCA described herein may generate impurities in the FDCA product. In some embodiments, the impurities may comprise 2-furoic acid. In some embodiments the molar ratio of FDCA to 2- furoic acid (i.e., the selectivity of the process for producing FDCA relative to 2-furoic acid) is least 5:1, or at least 6:1 or at least 7:1, or at least 8:1, or at least 9:1, or at least 10:1, or at least 15:1, or at least 20:1, or at least 25:1, or at least 30:1, or at least 35:1, or at least 40:1, or at least 45: 1, or at least 50: 1, or within any range defined by the aforementioned molar ratios.

IV. Hydrolysis of FDC A esters

[0142] In some embodiments, it may be desirable to perform a hydrolysis step subsequent to the cyclization and dehydration of the sugar derivative substrate in order to increase the yield of FDCA product. The cyclization and dehydration of the sugar derivative substrate may result in the formation of FDCA esters depending on the reaction conditions. For instance, ester formation may be observed when solvents containing one or more ether groups or alcohol groups are utilized, or when one or more alcohols are included in the reaction mixture. In particular, the Bronsted acid, either alone or in combination with the halide salt in the reaction mixture, may result in the degradation of an ether solvent, resulting in the formation of an alcohol, which may then be subsequently reacted with carboxylic acid groups from the C₆-aldaric acids in the sugar derivative substrate to form FDCA esters. This process may occur when the water-miscible organic solvent in the reaction mixture is 1,4- dioxane and the Bronsted acid is, e.g., HC1. Scheme 3 provides an illustrative example of how esters of FDCA may be formed in the presence of 1,4-dioxane (or any alcohol). Under acid conditions, 1,4 dioxane may undergo protonation at the oxygen atom followed by subsequent substitution to form a 2-haloethoxy ethanol, such as 2-(2-chloroethoxy)ethan-l-ol (CEE). The 2-haloethoxy ethanol (such as CEE) may then subsequently react to form esters with one or both of the carboxylic acid groups of the C₆-aldaric acids present in the sugar derivate substrate to form mono- and di-esters of FDCA. Alternatively, 2-haloethoxy ethanol (such as CEE) may react to form esters with one or both of the carboxylic acid groups of FDCA to form mono- and di-esters of FDCA. A subsequent base hydrolysis step may then be desired to generate a salt of FDCA. FDCA may then be regenerated via acidic workup. Similar formation of mono- and di-esters is not observed other solvents. For example the conversion of C₆-aldaric acids, or salts or lactone of C₆-aldaric acids to FDCA in, e.g., sulfolane, does not result in the formation of any appreciable quantities of FDCA esters. Scheme 3; Formation of FDCA and esters in 1,4-dioxane

[0143] In some embodiments, the hydrolysis step may be performed under basic conditions. In one embodiment, the base may comprise or consist of LiOH. In one embodiment, the base may comprise or consist of NaOH. In one embodiment, the base may comprise or consist of KOH. In one embodiment, the base may comprise or consist of CsOH. In one embodiment, the base may comprise or consist of Ca(OH)₂.

V. Purification of FDCA

[0144] The FDCA produced by one or more of the processes described herein may be purified from the reaction mixture. Purification of the FDCA may comprise or consist of separating any heterogeneous solids that may have formed in the reaction mixture. The reaction mixture may be further concentrated with respect to the soluble components by removal of a portion of the water-miscible organic solvent. Water-miscible organic solvent solvent removal may comprise or consist of evaporation (e.g., by using an evaporator), or distillation.

[0145] The FDCA may also be purified by crystallization. Thus, in some embodiments, the present disclosure provides for a process for producing a crystalline FDCA the method comprising: providing a crystallization solution comprising FDCA and a crystallization solvent; initiating crystallization of FDCA; and producing FDCA crystals.

[0146] As used herein, the term "crystallization solvent" refers to a solvent from which FDCA can be crystallized when conditions are imposed that cause a reduction in solubility of FDCA in the crystallization solvent (e.g., temperature reduction (cooling) or solvent removal). The crystallization solvent may comprise or consist of water, an organic solvent, or a multi-component solvent comprising water and/or a water-miscible organic solvent and/or two or more organic solvent species. The crystallization process may directly follow the dehydration reaction.

[0147] When crystallization follows the dehydration reaction, the crystallization solution is typically a solution comprising FDCA and the dehydration solvent. Crystallization may be performed by introducing a saturated (or super-saturated) solution of the FDCA reaction mixture in the dehydration solvent into a crystallizer in which the solution is subjected to crystallization conditions, and crystallization is initiated by, for example, lowering the temperature or concentrating the solution by solvent evaporation (i.e., solvent removal), or a combination of both. Solvent evaporation may be used to concentrate the solution to initiate crystallization, and may also be used to adjust the solvent composition to lower the solubility of FDCA. As used herein, the term "crystallization conditions" refers to an adjustment in temperature and/or adjustment in crystallization solution concentration and/or adjustment in crystallization solution composition that causes the initiation of crystallization of FDCA.

[0148] Cooling reduces the solubility of FDCA in the crystallization solvent, causing crystals of FDCA pathway product to form in the solution. The initial temperature of the solution is typically in the range of from or any number in between 60°C to 180°C, such as e.g., 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, or 180 °C or within a range defined by any two of the aforementioned temperatures. In some embodiments, the initial temperature of the solution is in the range from or any number in between 70°C to 150°C such as e.g., 70, 80, 90, 100, 110, 120, 130, 140, or 150 °C or within a range defined by any two of the aforementioned temperatures. When the crystallization solution is cooled, it is typically cooled to a temperature that is at or below 60°C, such as e.g., equal to or less than 60, 50, 40, 30, 20, 10, 5, or 0 °C or within a range defined by any two of the aforementioned temperatures. More typically, it is cooled to a temperature at or below 50°C or at or below 40°C such as, e.g., equal to or less than 50, 40, 30, 20, 10, 5, or 0 °C or within a range defined by any two of the aforementioned temperatures.

[0149] Seed crystals of FDCA may be added to further promote the initiation of crystallization. Other additives, such as anti-foaming agents or crystallization aids, may be added to the crystallization solution to promote the crystallization process, and facilitate the formation of a suspension containing FDCA crystals. Anti-foaming agents that are suitable for use in the practice of some of the alternatives described herein include, for example, silicones, surfactants, phosphates, alcohols, glycols, and/or stearates. Additives such as surfactants or electrolyte polymers may also influence the morphology and composition of the crystals formed. See, e.g., US 5,296,639 and US 6,534,680, which are hereby expressly incorporated herein by reference in their entireties. Other additives may function as a flow improver to prevent agglomeration of the crystalline product on storage (see for example US 6,534,680).

[0150] FDCA crystals produced by the processes described herein can be separated from the solution (mother liquor) by centrifugation, filtration, and/or other suitable process for separating solids from liquids. The crystals can then be washed and dried using any suitable process known to those having ordinary skill in the art.

VI. Integrated processes for converting lignocellulosic material to FDCA

[0151] The processes described herein may be conducted as integrated processes for carrying out the production of FDCA from lignocellulosic material. For example, lignocellulosic material may be subjected to hydrolysis conditions followed by oxidation conditions to produce a sugar derivative substrate, and the resulting sugar derivative substrate may be contacted with a Bronsted acid and a halide salt in the presence of a water-miscible organic solvent to form a reaction mixture thereby producing FDCA.

[0152] The processes of the present disclosure may be carried out in batch, semi- batch, or continuous reactor format using reactors, such as, for example, fixed bed reactors, trickle bed reactors, slurry phase reactors, and/or moving bed reactors. The relatively high solubilities of reactants and products (particularly, FDCA) in the water-miscible organic solvent facilitate the use of all such reactor formats, and particularly the fixed bed reactor format. [0153] The foregoing and other aspects of the disclosure may be better understood in connection with the following non-limiting examples.

EXAMPLES

[0154] Additional alternatives are disclosed in further detail in the following examples, which are not in any way intended to limit the scope of the claims.

EXAMPLE 1

Glucaric acid dilactone (GADL) to furan-2.5-dicaroxylic acid

(FDCA) in 0.25 mL format HQSS array

[0155] Salts, including FeBr₂ (Alfa Aesar), FeBr₃ (Alfa Aesar), CaBr₂ (Alfa Aesar), CuBr (Sigma Aldrich), CuBr₂ (Alfa Aesar), CuCl (Sigma Aldrich), Et₄NBr (Alfa Aesar), FeCl₃ (Sigma Aldrich), LiBr (Aldrich), Me₄NBr (Alfa Aesar), Me₄NCl (Acros Organics), NaBr (Aldrich), NiBr₂ (Alfa Aesar), ZnBr₂ (Alfa Aesar), ZnCl₂ (Sigma Aldrich), were transferred to 1.2 mL glass vials either as solids or by evaporation of a methanol solution containing the desired salt (0.1-0.5 mL) in a vacuum centrifuge (Genevac; 40-60 °C, 3-5 mbar, 1710 rpm, 3-5 h). The glass vials were placed within a 96- well reactor insert (Symyx) and charged with a glass bead to aid with mixing and 0.25 mL of a dioxane solution containing 0.2-0.6 M glucaric acid dilactone (GADL; in-house preparation), 0-2.0 M H₂0 (deionized (DI), 18.2 ΜΩ-cm), and 2.0-3.9 M HC1 (supplied as a 4.0 M HC1 solution in dioxane from Sigma- Aldrich). The reactor array was covered with a Teflon sheet, a silicone gasket sheet, and a Hastelloy-C gas diffusion plate each containing pinholes to allow gas diffusion. The closed reactor array was sealed in a pressure vessel (Symyx), pressurized to 300 psi N₂, heated to 120°C, and mixed with orbital shaking at a rate of 800 rpm for 3 h. After the desired reaction time, the pressure vessel was cooled to ambient temperature and vented. 0.75 mL of DMSO (BDH; 4-fold dilution) was added to each vial; the array was then sealed and inverted to mix. Each sample was then diluted 10-fold with a 0.25-1.2 M NaOH aqueous solution, mixed, and allowed to react for 0.5 h before a subsequent 5-fold dilution with DI H₂0. This sample preparation resulted in a 200-fold dilution of the reaction samples, which was required for analysis by high-performance liquid chromatography (HPLC; Agilent) with UV detection (λ = 254 nm) to determine the yield of furan-2,5-dicarboxylic acid (FDCA).

[0156] The results are presented in Table 1. The data shows that FDCA was produced using a variety of metal halide salts and tetraalkylammonium halide salts. The highest yields were observed for NaBr, ZnBr₂ and ZnCl₂.

Table 1

EXAMPLE 2

Glucaric acid dilactone (GADL) to furan-2.5-dicaroxylic acid

(FDCA) in 2.0 mL format HQSS array

[0157] A similar experimental procedure to Example 1 was used to test reaction solutions of 2.0 mL quantities. Salts, including Bu₄NBr (Acros Organics), E NBr (Alfa Aesar), Me₄NBr (Alfa Aesar), Me4NCl (Acros Organics), Me₄NOAc (Acros Organics), NaBr (Aldrich), ZnCl₂ (Sigma Aldrich), were transferred as solids to 4.0 mL glass vials. These glass vials were placed within a 24-well reactor insert (Symyx) and charged with three glass beads to aid with mixing and 2.0 mL of a dioxane solution containing 0.2 M GADL (in- house preparation) and 3.3-3.6 M HC1 (supplied as a 4.0 M HC1 solution in dioxane from Sigma Aldrich). The reactor was covered with a Teflon sheet, silicone gasket, Teflon sheet, and a stainless-steel diffusion plate each containing pinholes to allow gas diffusion. The closed reactor array was sealed in a pressure vessel (Symyx), pressurized to 300 psi N₂, heated to 90°C or 120°C, and mixed with orbital shaking at a rate of 500 rpm or 800 rpm for 17 h or 3 h, respectively. After the desired reaction time, the pressure vessel was cooled to ambient temperature and vented. 2.0 mL of DMSO (BDH; 2-fold dilution) was then added to each vial, and the vials were capped and shaken. Each sample was then diluted another 2-fold with DMSO, followed by a 10-fold dilution with 0.5-1 M NaOH aqueous solution. Samples were shaken and allowed to react for 0.5 h before a subsequent 5-fold dilution with DI H₂0. This sample preparation resulted in a 200-fold dilution of the crude reaction mixture, which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA.

[0158] The results are presented in Table 2. The data shows that FDCA was produced using a variety of metal halide salts and tetraalkylammonium halide salts. The highest yields were observed for NaBr and ZnCl₂. Table 2

EXAMPLE 3

Glucaric acid dilactone (GADL) to furan-2.5-dicaroxylic acid (FDCA)

in 2.0-3.0 mL format screw-top pressure vessels

[0159] Experiments were also performed in sealed vials (8 mL glass vials or 15 mL glass pressure vessels; Chemglass). ZnCl₂ (Sigma Aldrich) was transferred by mass to each vial, and then 2.0-3.0 mL of 0.2 M GADL and 3.5 M HC1 in dioxane and a magnetic stir bar were added to each vial. The vials were heated to 90°C in a silicone oil bath and reaction solutions were stirred at a rate of 400-500 rpm. After the desired reaction time, the vials were cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 10-fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 5-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 200-fold, which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA.

[0160] The results are presented in Table 3. FDCA yields approaching 90 percent were observed for reaction times of 18 h or greater.

Table 3

EXAMPLE 4

Reactions of glucaric acid dilactone (GADL) to furan-2.5-dicaroxylic acid (FDCA) in the absence of salts or promoters

[0161] FDCA yields were also measured in GADL-HCl-dioxane mixtures without salt or H₂0 present. These experiments were performed following the protocols outlined in Examples 1 and 2.

[0162] The results are presented in Table 4. The data demonstrates that the yields of FDCA from GADL are significantly lower when no salts or promotors (e.g. H₂0) are present in the reaction mixture.

Table 4

EXAMPLE 5

Effect of H2O on reactions of glucaric acid dilactone (GADL) with HCl/HBr

[0163] FDCA yields were also measured in GADL-H₂0-(HCl/HBr)-dioxane mixtures without salt present. These experiments were performed following the protocols outlined in Examples 1 and 2.

[0164] The results are presented in Table 5. The data shows that the addition of water may lead to an increase in FDCA yield.

Table 5

EXAMPLE 6

Effect of alcohol additives on reactions of glucaric acid dilactone (GADL) with HC1

[0165] FDCA yields were also measured in GADL-alcohol-HCl-dioxane mixtures without salt present. The alcohols used include n-butanol (Acros Organics) and 2- (2-chloroethoxy)ethanol (CEE; Acros Organics). These experiments were performed following the protocols outlined in Examples 1 and 2.

[0166] The results are presented in Table 6. Increases in yields are observed by adding an alcohol to the reaction mixture. CEE is also generated to some extent during the reaction mixture via the acid-catalyzed cleavage of 1,4-dioxane.

Table 6

EXAMPLE 7

Effect of ZnCh additives on FDCA yields form additional substrates

in HCl-dioxane reaction mixture

[0167] Experiments using different starting substrates were performed according to the protocols outlined in Example 3. The substrates investigated included: glucaric acid dilactone (GADL; in-house preparation), 1,4-glucaric acid monolactone (1,4-GAML; Sigma), K-glucarate (Pfaltz and Bauer Inc.), and galactaric acid (Alfa Aesar). For these experiments, the temperature of the silicone oil bath containing the reaction vessels was increased in a series of steps (50°C, 0.5 h; 70°C, 0.5 h; 90°C, 0.5 h) before reaching the reaction temperature (120°C, 3h) as opposed to placing the reaction vessels into the silicone oil bath preheated to the desired reaction temperature (Example 3). Subsequent reaction sample work-up and product analysis was performed similar to Example 3.

[0168] The results from these experiments are presented in Table 6. The data shows the profound effect of adding ZnCl₂ to the reaction mixture. For example, Reactions 84 and 85 show that the addition of ZnCl₂ results in an almost 5-fold increase in FDCA yield (18% to 82%). Improvements in yield are also observed for other substrates such as potassium glucarate (Reactions 87 and 88) and galactaric acid (Reactions 89 and 90).

Table 7

EXAMPLE 8

Glucaric Acid dilactone (GADL) to furan-2.5-dicaroxylic acid (FDCA)

in 2.0 mL format HQSS array

[0169] A similar experimental procedure to Examples 1 and 2 was used to test reaction solutions of 2.0 mL quantities. Salts, including Et₄NBr (Alfa Aesar), Me₄NBr (Alfa Aesar), MgBr₂ (Acros Organics), CaBr₂ (Alfa Aesar), LiBr (Aldrich), were transferred as solids to 4.0 mL glass vials. These glass vials were placed within a 24-well reactor insert (Symyx) and charged with three glass beads to aid with mixing and 2.0 mL of a sulfolane (Sigma-Aldrich) solution containing 0.2-1.2 M GADL (in-house preparation) and 0.15-6.0 M mineral acid, including MsOH (Acros Organics), H₂S0₄ (Sigma-Aldrich), HC1 (J.T. Baker), HBr (Alfa Aesar). The reactor was covered with a Teflon sheet, silicone gasket, Teflon sheet, and a stainless-steel diffusion plate each containing pinholes to allow gas diffusion. The closed reactor array was sealed in a pressure vessel (Symyx), pressurized to 300 psi N₂, heated to 100°C or 120°C, and mixed with orbital shaking at a rate of 500 rpm or 800 rpm for 17 h or 3 h, respectively. After the desired reaction time, the pressure vessel was cooled to ambient temperature and vented. 2.0 mL of DMSO (BDH; 2-fold dilution) was then added to each vial, and the vials were capped and shaken. Each sample was then diluted another 2- fold with DMSO, followed by a 10-fold dilution with 0.05-1 M NaOH aqueous solution. Samples were shaken and allowed to react for 0.5 h before an aliquot of this base-hydrolyzed sample was then further diluted with DI H₂0 to a final nominal concentration of 1 mM (e.g. a solution with an initial GADL concentration of 0.4 M would require an additional lOx dilution with DI H₂0 to reach a total dilution of 400x by volume). These samples were then analyzed by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA.

[0170] The results are presented in Table 8. The data shows that good FDCA yields are achieved in sulfolane for a variety of salts and acids. Table 8

EXAMPLE 9

Reactions of GADL in sulfolane and H2O with mineral acids in absence of

other catalysts or promoters

[0171] FDCA yields were also measured in GADL-mineral acid-sulfolane and GADL-mineral acid-H₂0 mixtures without salt present, where mineral acids include: MsOH (Acros Organics), H₂S0₄ (Sigma-Aldrich), HC1 (J.T. Baker), HBr (Alfa Aesar). These experiments were performed following the protocols outlined in Examples 1 and 2.

[0172] The results are presented in Table 9. The data shows that FDCA yields are significantly lower in the absence of halide salts, even when using high concentrations of acid and long reaction times.

EXAMPLE 10

Glucaric Acid dilactone (GADL) to furan-2.5-dicaroxylic acid (FDCA) in 2.0-3.0 mL format screw-top pressure vessels

[0173] Experiments were performed in sealed vials (15 mL glass pressure vessels; Chemglass). Reactions were run with 0.2 M GADL in sulfolane with 4.0 M H₂S0₄. To each vial was added desired masses of GADL, then sulfolane. To the mixture was added H₂S0₄ by volume and a magnetic stir bar was added to each vial. The vials were sealed and placed in a silicone oil bath pre-heated to desired reaction temperature. The reaction mixtures were stirred at a rate of 400-500 rpm. After the desired reaction time, the vials were cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 10-fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 5-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 200-fold, which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA. [0174] The results are presented in Table 10. The data shows that FDCA yields in the range of 60%-70% were obtained using sulfolane as the solvent and H₂S0₄ as the acid. In the absence of salts, reaction times of 24 hours or longer were used.

Table 10

EXAMPLE 11

Glucaric acid dilactone (GADL) to furan-2.5-dicarboxvlic acid (FDCA)

in 2.0 mL format screw-top pressure vessels

[0175] Experiments were performed in sealed vials (15 mL glass pressure vessels; Chemglass). Reactions were run with 0.4 M GADL in sulfolane with 1.0 or 2.0 M MsOH and 0.8, 1.2 or 1.6 M LiBr. To each vial was added desired masses of GADL, halide salt, and sulfolane in the order mentioned. To the mixture was added methanesulfonic acid (MsOH) by volume and a magnetic stir bar was added to each vial. The vials were sealed and placed in a silicone oil bath pre-heated to desired reaction temperature. The reaction mixtures were stirred at a rate of 400-500 rpm. After the desired reaction time, the vials were cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 2-fold DMSO dilution and a subsequent 10-fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 5-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 400-fold which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA.

[0176] The results are presented in Table 11. The data below demonstrates that the addition of halide salts, e.g., LiBr, to the reaction mixture results in an increased yield of FDCA. Moreover, yields of over 80% are achievable with reaction times as short as 2 hours.

Table 11

EXAMPLE 12

FDCA yields from additional substrates in sulfolane with MsQH and CaBr¾

2.0 mL format in screw-top pressure vessels

[0177] Experiments were performed in sealed vials (15 mL glass pressure vessels; Chemglass). Reactions were run with 0.4 M substrate in sulfolane with 1.0 M MsOH and 0.8 M CaBr₂. The substrates investigated included: glucaric acid dilactone (GADL; in-house preparation), 1,4-glucaric acid monolactone (1,4-GAML; Sigma), 3,6-glucaric acid monolactone (3,6-GAML; in-house preparation), glucaric acid dilactone diacetate (DL-DA; in-house preparation), K-glucarate (Pfaltz and Bauer Inc.), calcium glucarate tetrahydrate and galactaric acid (Alfa Aesar). To each vial was added desired masses of substrates, CaBr₂ and sulfolane in the order mentioned. To the mixture was added MsOH by volume and a magnetic stir bar was added to the vial. The vial was sealed and placed in a silicone oil bath pre-heated to 120 °C. The reaction mixture was stirred at a rate of 400-500 rpm. After the desired reaction time, the vial was cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 2-fold DMSO dilution and a subsequent 10-fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 5-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 400-fold which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA.

[0178] The results are presented in Table 12. The data shows that a variety of substrates can be used to form FDCA in high yield, including glucaric acid dilactone, 1,4- glucaric acid monolactone, and potassium glucarate.

Table 12

EXAMPLE 13

Comparison of FDCA yields with and without base hydrolysis

[0179] The results presented in Table 13 show selected reactions conducted in a dioxane-HCl system and in a sulfolane-MsOH system. Reactions in 1,4-dioxane-HCl may lead to the formation of a 2-chloroethoxyethanol, which may subsequently form mono- and di-esters of FDCA.

Table 13

EXAMPLE 14

Glucaric acid dilactone (GADL) to furan-2.5-dicarboxvlic acid (FDCA)

[0180] Experiments were performed in sealed vials. Reactions were run with GADL in sulfolane with a salt selected from CaBr₂, CaCl₂, CeBr₃, CuBr₂, LiBr, LiCl, MgBr₂, NaBr, ZnBr₂, ZnCl₂, NH₄Br, tetrabutylammonium bromide, tetraethylammonium bromide, tetraethylammonium chloride, tetramethylammonium bromide, and tetramethylammonium hydrogen sulfate. To each vial was added GADL, halide salt, and sulfolane. To the mixture was added a Bronsted acid selected from HBr, HC1, H₂S0₄, MsOH and CF₃S0₃H (TfOH). The vials were sealed and heated. The reaction mixtures were stirred. After the reaction, the vials were cooled to ambient temperature.

[0181] The results are presented in Figures 1A-1F, 2A-2F, 3A-3F and 4.

EXAMPLE 15

Screening effects of salt, acid, and water concentrations on the selective conversion of

GADL to FDCA in Sulfolane

[0182] Experiments were performed in glass vials. Reactions were run with 0.4 M glucaric acid dilactone sugar derivative substrate in 2.0 mL sulfolane with the following: 0.05, 0.1, 0.2 or 0.4 M CaBr₂ or 0.2, 0.4, or 0.8 M MgBr₂; 0.05, 0.15, or 0.25 M H₂S0₄ or 0.5 M MsOH; and either 0 or 1 M H₂0 for CaBr₂ vials or 0 or 0.5 M H₂0 for MgBr₂ vials. These glass vials were placed within a 24-well reactor insert (Symyx) and charged with three glass beads to aid with mixing. The reactor was covered with a Teflon sheet, silicone gasket, Teflon sheet, and a stainless- steel diffusion plate each containing pinholes to allow gas diffusion. The closed reactor array was sealed in a pressure vessel (Symyx), pressurized to 300 psi N₂, heated to 100 °C, and mixed with orbital shaking at a rate of 500 rpm for 17 h. After the desired reaction time, the vials were cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 2-fold DMSO dilution and a subsequent 10-fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 5-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 400-fold which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA. [0183] The results are shown in Figures 5-9.

EXAMPLE 16

GADL to FDCA in Sulfolane

[0184] Experiments were performed in glass vials. Reactions were run with 0.4 M glucaric acid dilactone sugar derivative substrate in 2.0 mL sulfolane with the following: 0.2, 0.4 or 0.6 M MgBr₂, 0.2, 0.4, or 0.8 CaBr₂, or 1.0, 1.6 or 2 M LiBr; 0.25 M H₂S0₄, 0.5 M HC1 or 0.5 M HBr; and 2.5 M H₂0 for HC1 and HBr containing vials. These glass vials were placed within a 24- well reactor insert (Symyx) and charged with three glass beads to aid with mixing. The reactor was covered with a Teflon sheet, silicone gasket, Teflon sheet, and a stainless- steel diffusion plate each containing pinholes to allow gas diffusion. The closed reactor array was sealed in a pressure vessel (Symyx), pressurized to 300 psi N₂, heated to 120 °C, and mixed with orbital shaking at a rate of 800 rpm for 3 h. After the desired reaction time, the vials were cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 2-fold DMSO dilution and a subsequent 10- fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 5-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 400-fold which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA.

[0185] The results are shown in Figures 10, 1 lA-1 ID, and 12-13.

EXAMPLE 17

Glucaric Acid dilactone (GADL) to furan-2.5-dicaroxylic acid

(FDCA) in 0.25 mL format HQSS array

[0186] Experiments were performed in glass vials (1.2 mL vials; Chemglass). The vials were charged with 0.2 M glucaric acid dilactone sugar derivative substrate in 0.25 mL water-miscible organic solvent selected from dioxane or NMP, and with an acid selected from HC1, HBr, MsOH, and H₂S0₄. Water and tetraethylammonium bromide (TEAB) were optionally added to the reaction vials, The reactor array was covered with a Teflon sheet, a silicone gasket sheet, and a Hastelloy-C gas diffusion plate each containing pinholes to allow gas diffusion. The closed reactor array was sealed in a pressure vessel (Symyx), pressurized to 300 psi N₂, heated to 120°C, and mixed with orbital shaking at a rate of 800 rpm for 3 h. After the desired reaction time, the pressure vessel was cooled to ambient temperature and vented. 0.75 mL of DMSO (BDH; 4-fold dilution) was added to each vial; the array was then sealed and inverted to mix. Each sample was then diluted 10-fold with a 0.25-1.2 M NaOH aqueous solution, mixed, and allowed to react for 0.5 h before a subsequent 5-fold dilution with DI H₂0. This sample preparation resulted in a 200-fold dilution of the reaction samples, which was required for analysis by high-performance liquid chromatography (HPLC; Agilent) with UV detection (λ = 254 nm) to determine the yield of furan-2,5-dicarboxylic acid (FDCA).

[0187] The results are shown in Figures 14-19.

EXAMPLE 18

Glucaric Acid dilactone (GADL) to furan-2.5-dicaroxylic acid (FDCA) in 0.25 mL format HQSS array - Investigation of the use of TEAS and TEAC at lower concentrations and reaction temperatures

[0188] Experiments were performed in glass vials (1.2 mL vials; Chemglass). The vials were charged with 0.2 M glucaric acid dilactone sugar derivative substrate in 0.25 mL dioxane, 3.6 M HC1, and a halide salt selected from TEAB or TEAC. Water was optionally added to the reaction vials, The reactor array was covered with a Teflon sheet, a silicone gasket sheet, and a Hastelloy-C gas diffusion plate each containing pinholes to allow gas diffusion. The closed reactor array was sealed in a pressure vessel (Symyx), pressurized to 300 psi N₂, heated to 90°C, and mixed with orbital shaking at a rate of 500 rpm for 16 h. After the desired reaction time, the pressure vessel was cooled to ambient temperature and vented. 0.75 mL of DMSO (BDH; 4-fold dilution) was added to each vial; the array was then sealed and inverted to mix. Each sample was then diluted 10-fold with a 0.25-1.2 M NaOH aqueous solution, mixed, and allowed to react for 0.5 h before a subsequent 5-fold dilution with DI H₂0. This sample preparation resulted in a 200-fold dilution of the reaction samples, which was required for analysis by high-performance liquid chromatography (HPLC; Agilent) with UV detection (λ = 254 nm) to determine the yield of furan-2,5-dicarboxylic acid (FDCA).

[0189] The results are shown in Figures 20-27.

EXAMPLE 19

Dehydration of mannaric acid dilactone (MADL) to furan-2.5-dicarboxvlic acid (FDCA) using methanesulfonic acid in 1.0 mL reaction mixture

[0190] The experiments were performed in a glass vial (4 mL vials Chemglass). Mannaric acid dilactone (MADL) was prepared from mannose according to the method described in Ponder et al., International Patent Publication No. WO 00/34211. LiBr, CaBr₂*xH₂0, MgBr₂*6H₂0, MgBr₂ anhyd., MsOH, and sulfolane were purchased from Sigma Aldrich and used without further purification. The vials were charged with MADL and the respective bromide salt followed by sulfolane to make 1 mL of reaction mixture with the correct concentrations. To the mixture was added MsOH by weight and a magnetic stir bar was added to the vial. The vial was sealed and placed in a silicone oil bath pre-heated to 120 °C. The reaction mixture was stirred at a rate of 400-500 rpm. After the desired reaction time, the vial was cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 10-fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 10-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 400-fold which was required for analysis by HPLC (W aters) with UV detection (λ = 254 nm) and a Hypercarb column (Thermo Scientific) to determine the yield of FDCA.

[0191] The results presented in Table 14 show selected mannaric acid dilactone (MADL) to furan-2,5-dicarboxylic acid (FDCA) dehydration reactions using methanesulfonic acid.

Table 14: Mannaric acid dilactone, methanesulfonic acid

EXAMPLE 20

Dehydration of mannaric acid dilactone (MADL) to furan-2.5-dicarboxvlic acid

(FDCA) using hydrogen bromide in 1.0 mL reaction mixture

[0192] The experiments were performed in a glass vial (4 mL vials Chemglass). Mannaric acid dilactone (MADL) was prepared from mannose according to the method described in Ponder et al., International Patent Publication No. WO 00/34211. CaBr₂*xH₂0, MgBr₂ anhyd., HBr (48% aq.), and sulfolane were purchased from Sigma Aldrich and used without further purification. A stock solution of the bromide salt, HBr (48% aq.) in sulfolane was heated to 120 °C until everything dissolved (15-20 min). The stock solution was cooled to RT and MADL was added and the suspension was stirred until MADL dissolved. 1.0 mL was transferred to each reaction vial. The vials were sealed and placed in a silicone oil bath pre-heated to 120 °C. The reaction mixtures were stirred at a rate of 400-500 rpm. After the desired reaction time, the vials were cooled to ambient temperature. A 4-fold DMSO dilution was added and the vials were shaken. This was followed by a 10-fold dilution with 0.25 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 10-fold dilution with DI H₂0 of the resulting sample brought the final dilution to 400-fold which was required for analysis by HPLC (Waters) with UV detection (λ = 254 nm) and a Hypercarb column (Thermo Scientific) to determine the yield of FDCA.

[0193] The results presented in Table 15 show selected mannaric acid dilactone (MADL) to furan-2,5-dicarboxylic acid (FDCA) dehydration reactions using hydrogen bromide.

Table 15: Mannaric acid dilactone, hydrogen bromide

EXAMPLE 21

Dehydration of mixed aldaric acids aldaric dilactones to furan-2.5-dicarboxvlic acid

(FDCA) in 1.0 mL reaction mixture

[0194] The results presented in Table 16 show selected mixed aldaric acids/aldaric dilactones to furan-2,5-dicarboxylic acid (FDCA) dehydration reactions using methanesulfonic acid and hydrogen bromide. Mixed alderic acids and aldaric dilactones may include mannaric acid dilactone (MADL), glucaric acid dilactone (GADL) and galactaric acid (GA).

[0195] For the procedure for reactions using MgBr₂ and MsOH, see Example 20: Dehydration of mannaric acid dilactone (MADL) to furan-2,5-dicarboxylic acid (FDCA) using methanesulfonic acid in 1.0 mL reaction mixture.

[0196] For the procedure for reactions using MgBr₂ and HBr, see Example 21: Dehydration of mannaric acid dilactone (MADL) to furan-2,5-dicarboxylic acid (FDCA) using hydrogen bromide in 1.0 mL reaction mixture.

Table 16: Mixed aldaric acids

EXAMPLE 22

Glucaric acid dilactone (GADL) to furan-2.5-dicarboxvlic acid (FDCA) in 4.0 mL format screw-top pressure vessels

[0197] Further experiments were performed in sealed vials (15 mL glass pressure vessels; Chemglass). Reactions were run with 1.25 M glucaric acid dilactone (GADL) in sulfolane with 1.0 M HBr (Alfa Aesar) and 0.94 M MgBr₂ (Aldrich). Into each vial desired masses of MgBr₂, a sulfolane solution containing MgBr₂ and HBr (0.83 M and 1.64 M, respectively; in-house preparation), and a sulfolane solution containing 3.4 M GADL (in-house preparation) were added in the order mentioned. A magnetic stir bar was added to each vial. The vials were sealed and placed in a silicone oil bath pre-heated to a desired reaction temperature and allowed 0.083 h (or about 5 min) to reach reaction temperature. The reaction mixtures were stirred at a rate of 600-1000 rpm. After the desired reaction time, the vials were cooled to ambient temperature. A 3-fold DMSO dilution was added and the vials were shaken. This was followed by a 4-fold DMSO dilution and a subsequent 10-fold dilution with 0.06 M NaOH aqueous solution; vials were then shaken and sat for 0.5 h at ambient temperature. A 10- fold dilution with DI H₂0 of the resulting sample brought the final dilution to 1200-fold which was required for analysis by HPLC (Agilent) with UV detection (λ = 254 nm) to determine the yield of FDCA.

[0198] The results presented in Table 17 show selected glucaric acid dilactone (GADL) to furan-2,5-dicarboxylic acid (FDCA) dehydration reactions, and Reactions 230-241 demonstrate that the increase in reaction temperature results in a decrease in required reaction time.

Table 17: Glucaric acid dilactone

[0199] While preferred embodiments of the disclosure have been illustrated and described, it will be appreciated that various changes can be made therein without departing from the spirit and scope of the disclosure. Therefore it should be clearly understood that the forms disclosed herein are illustrative only and are not intended to limit the scope of the present disclosure.

Claims

WE CLAIM:

1. A process for producing 2,5-furandicarboxylic acid (FDCA), the process comprising contacting a sugar derivative substrate with a Bronsted acid and a halide salt in the presence of a water-miscible organic solvent to form a reaction mixture, and producing FDCA.

2. The process of claim 1, wherein the sugar derivative substrate is a homogenous sugar derivative substrate.

3. The process of claim 1, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate.

4. The process of any one of claims 1 to 3, wherein the sugar derivative substrate is selected from the group consisting of: glucaric acid and salts and lactones thereof; galactaric acid and salts and lactones thereof; and mannaric acid and salts and lactone thereof; or a mixture thereof.

5. The process of claim 4, wherein the sugar derivative substrate is selected from the group consisting of glucaric acid, glucaric acid dilactone, 1,4-glucaric acid monolactone, 3,6-glucaric acid monolactone, sodium glucarate, potassium glucarate, calcium glucarate, galactaric acid, 1,4-galactaric acid monolactone, 3,6-galactaric acid monolactone, sodium galactarate, potassium galactarate, calcium galactrate, mannaric acid, mannaric acid dilactone, 1,4-mannaric acid monolactone, 3,6-mannaric acid monolactone, sodium mannarate, potassium mannarate, calcium mannarate, or a mixture thereof.

6. The process of claim 4, wherein the sugar derivative substrate is glucaric acid, or a salt or lactone thereof.

7. The process of claim 4, wherein the sugar derivative substrate is galactaric acid, or a salt or lactone thereof.

8. The process of claim 4, wherein the sugar derivative substrate is mannaric acid, or a salt or lactone thereof.

9. The process of claim 4, wherein the sugar derivative substrate is glucaric acid dilactone.

10. The process of claim 4, wherein the sugar derivative substrate is mannaric acid dilactone.

11. The process of claim 4, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate comprising glucaric acid dilactone and mannaric acid dilactone.

12. The process of claim 4, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate consisting of glucaric acid dilactone and mannaric acid dilactone.

13. The process of claim 4, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate comprising glucaric acid dilactone, mannaric acid dilactone, and galactaric acid.

14. The process of claim 4, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate consisting of glucaric acid dilactone, mannaric acid dilactone, and galactaric acid.

15. The process of any one of claims 1 to 14, wherein the Bronsted acid is selected from the group consisting of hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, phosphoric acid, methanesulfonic acid, p-toluenesulfonic acid, benzenesulfonic acid, trifluoromethanesulfonic acid, acetic acid, and trifluoracetic acid.

16. The process of claim 15, wherein the Bronsted acid is selected from the group consisting of hydrochloric acid, hydrobromic acid, sulfuric acid, and methanesulfonic acid.

17. The process of any one of claims 1 to 16, wherein the halide salt is a metal halide or a tetraalkylammonium halide.

18. The process of claim 17, wherein the metal halide is selected from the group consisting of FeBr₂, FeBr₃, FeCl₂, FeCl₃, CuBr, CuBr₂, CuCl, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, NaCl, NaBr, Nal, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, MgBr₂, KC1, KBr, and KI.

19. The process of claim 18, wherein the metal halide salt is selected from the group consisting of FeBr₂, FeCl₂, CuBr₂, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, and MgBr₂.

20. The process of any one of claims 1 to 18, wherein the metal halide salt is CaBr₂ and the Bronsted acid is hydrobromic acid.

21. The process of any one of claims 1 to 18, wherein the metal halide salt is CaBr₂ and the Bronsted acid is hydrochloric acid.

22. The process of any one of claims 1 to 18, wherein the metal halide salt is CaBr₂ and the Bronsted acid is methanesulfonic acid.

23. The process of any one of claims 1 to 18, wherein the metal halide salt is CaBr₂ and the Bronsted acid is sulfuric acid.

24. The process of any one of claims 1 to 18, wherein the metal halide salt is MgBr₂ and the Bronsted acid is hydrobromic acid.

25. The process of any one of claims 1 to 18, wherein the metal halide salt is MgBr₂ and the Bronsted acid is methanesulfonic acid.

26. The process of any one of claims 1 to 18, wherein the metal halide salt is MgBr₂ and the Bronsted acid is sulfuric acid.

27. The process of any one of claims 1 to 18, wherein the metal halide salt is LiBr and the Bronsted acid is hydrobromic acid.

28. The process of any one of claims 1 to 18, wherein the metal halide salt is LiBr and the Bronsted acid is methanesulfonic acid.

29. The process of any one of claims 1 to 18, wherein the metal halide salt is ZnCl₂ and the Bronsted acid is hydrochloric acid.

30. The process of claim 17, wherein the tetraalkylammonium halide is selected from the group consisting of tetramethylammonium chloride, tetramethylammonium bromide, tetraethylammonium chloride, tetraethylammonium bromide, tetrabutylammonium chloride, and tetrabutylammonium bromide.

31. The process of any one of claims 1 to 17 or 30, wherein the tetraalkylammonium halide salt is tetraethylammonium bromide and the Bronsted acid is methanesulfonic acid.

32. The process of any of claims 1 to 31, wherein the water-miscible organic solvent is selected from the group consisting of 1,4-dioxane, tetrahydrofuran, sulfolane, a glyme, N-methyl-2-pyrrolidone, methyl ethyl ketone, dimethyl formamide, and dimethyl sulfoxide.

33. The process of claim 32, wherein the water-miscible organic solvent is 1,4-dioxane or sulfolane.

34. The process of claim 32, wherein the glyme is selected from the group consisting of 1,2-dimethoxyethane, ethyl glyme, diethylene glycol dimethyl ether, ethyl diglyme, triglyme, butyl diglyme, tetraglyme, and a polyglyme.

35. The process of any one of claims 1 to 32, the process further comprising pressurizing the reaction mixture to a pressure ranging from 15-500 psi, 25-500 psi, 50- 500 psi, 100-500 psi, 200-500 psi, 300-500 psi, or 400-500 psi or within a range defined by any two of the aforementioned pressures.

36. The process of any one of claims 1 to 35, wherein the concentration of the sugar derivative substrate is in the range from 0.01 M to 10.0 M.

37. The process of claim 36, wherein the concentration of acid ranges from between 0.01-10.0 M, 0.02-5.0 M, 0.05-2.0 M, 0.10-1.0 M, 0.15-1.0 M, 0.20-1.0 M, 0.2- 1.25 M, 0.4-1.25 M, 0.5-1.0 M, or 0.6-1.25 M, or within a range defined by any two of the aforementioned concentrations

38. The process of any one of claims 1 to 37, wherein the concentration of acid is in the range from 0.05 M to 10.0 M.

39. The process of claim 38, wherein the concentration of acid ranges from between 0.05-10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or within a range defined by any two of the aforementioned concentrations.

40. The process of any one of claims 1 to 39, wherein the concentration of halide salt ranges from between 0.01-3.0 M, 0.05-2.0 M, 0.1-1.0 M, or 0.2-0.5 M, or within a range defined by any two of the aforementioned concentrations.

41. The process of claim 38, wherein the concentration of halide salt is at least

0.1 M.

42. The process of claim 40, wherein the concentration of halide salt is less than 2.0 M, or less than 1.5 M, or less than 1 M, or less than 0.75 M, or less than 0.5 M but not zero.

43. The process of any one of claims 1 to 42, the process further comprising adding water to the reaction mixture.

44. The process of claim 43, wherein the concentration of water ranges from between 0.01- 20.0 M, 0.01- 10.0 M, 0.1-5.0 M, or 0.2-1.0 M, or within a range defined by any two of the aforementioned concentrations.

45. The process of any one of claims 1 to 44, the process further comprising adding alcohol to the reaction mixture.

46. The process of claim 45, wherein the alcohol is selected from the group consisting of n-butanol, sec-butanol, isobutanol, 1-pentanol, 2-pentanol, 2-(2- chloroethoxy)ethanol), ethoxyethanol, and cyclohexanol.

47. The process of claim 45 or claim 46, wherein the concentration of alcohol ranges from between 0.01-1.0 M, 0.1-l.OM, or 0.5-1.0M, or within a range defined by any two of the aforementioned concentrations.

48. The process of any one of claims 37 to 47, wherein the reaction mixture is pressurized with one or more gasses selected from the group consisting of nitrogen, argon, helium, and carbon dioxide.

49. The process of any one of claims 1 to 48, wherein the reaction mixture is heated to a temperature range from between 90-200 °C, 110-160 °C, 110-180 °C, 130-160 °C, 70-150 °C, 80-150 °C, 90-150 °C, 100-150 °C, 110-150 °C, 120-150 °C, 130-150 °C, or 140-150 °C or within a range defined by any two of the aforementioned temperatures.

50. The process of claim 49, wherein the reaction mixture is heated to a temperature of 90 °C.

51. The process of claim 49, wherein the reaction mixture is heated to a temperature of 120 °C.

52. The process of claim 49, wherein the reaction mixture is heated to a temperature of 140 °C.

53. The process of claim 49, wherein the reaction mixture is heated to a temperature of 160 °C.

54. The process of any one of claims 1 to 53, wherein the concentration of sugar derivative substrate ranges from between 0.05-10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or within a range defined by any two of the aforementioned concentrations.

55. The process of any one of claims 1 to 54, wherein the reaction mixture is heated for 1 min to 24 hours, 1 min to 3 hours, 1 min to 0.5 hours, 0.5-96 hours, 1-96 hours, 2-72 hours, 5-48 hours, 1-24 hours, 2-24 hours, 12-24 hours, or 20-24 hours or for a time that is within a range defined by any two of the aforementioned times, such as 1 min., 2 min., 3 min., 4 min., 5 min., 6 min., 7 min., 8 min., 9 min., or 10 min., or for a time that is within a range defined by any two of the aforementioned times.

56. The process of any one of claims 1 to 55, wherein 2-furoic acid is formed.

57. The process of any one of claims 1 to 56, wherein the water-miscible organic solvent is dioxane, and the process further comprises:

forming a 2-haloethoxy ethanol; and

reacting the 2-haloethoxy ethanol with FDCA to form a mono- or di-ester of FDCA.

58. The process of claim 57, the process further comprising hydrolyzing the FDCA ester with a base to form an FDCA salt.

59. The process of claim 58, wherein the base is selected from the group consisting of NaOH, KOH, LiOH, Ca(OH)₂, and CsOH.

60. The process of any one of claims 1 to 59, wherein the process further comprises preparing the sugar derivative substrate from lignocellulosic material by subjecting the lignocellulosic material to hydrolysis conditions followed by oxidation conditions to produce a sugar derivative substrate.

61. The process of claim 60, wherein the hydrolysis of the lignocellulosic material produces a sugar derivative substrate comprising a mixture of C6-aldaric acids.

62. The process of any one of claims 1 to 61, wherein the lignocellulosic material comprises a compound selected from the group consisting of cellulose, hemicellulose, and lignin.

63. The process of any one of claims 1 to 62, wherein the yield of FDCA is at least 60%, or at least 70%, or at least 80%, or at least 90%, or at least 95%, or at least 98%, or at least 99% or within a range defined by any two of the aforementioned percentages.

64. The process of any one of claims 1 to 62, wherein the yield of FDCA is at least 60%, or at least 70%, or at least 80%, or at least 90%, or at least 95%, or at least 98%, or at least 99% or within a range defined by any two of the aforementioned percentages.

65. The process of any one of claims 1 to 62, wherein the process produces FDCA and additional impurities, and wherein the amount of FDCA relative to the additional impurities is at least 60%, or at least 65%, or at least 70%, or at least 75%, or at least 80%, or at least 85%, or at least 90%, or at least 91%, or at least 92%, or at least 93%, or at least 94%, or at least 95%, or at least 96%, or at least 97%, or at least 98%, or at least 99% by weight percent, or within any range defined by the aforementioned weight percents.

66. The process of any one of claims 1 to 62, wherein the process produces FDCA and additional 2-furoic acid impurities, wherein the molar ratio of FDCA to 2- furoic acid is least 5:1, or at least 6:1 or at least 7:1, or at least 8:1, or at least 9:1, or at least 10:1, or at least 15:1, or at least 20:1, or at least 25:1, or at least 30:1, or at least 35:1, or at least 40:1, or at least 45:1, or at least 50:1, or within any range defined by the aforementioned molar ratios.

67. The process of any one of claims 1 to 65, the process further comprising steps of isolating, crystalizing, or decolorizing said FDCA.

68. The product formed by the process of any one of claims 1 to 67.

69. A reaction mixture comprising:

(a) a sugar derivative substrate;

(b) a water-miscible organic solvent;

(c) a halide salt; and

(d) a Bronsted acid.

70. The reaction mixture of claim 69, wherein the sugar derivative substrate is a homogenous sugar derivative substrate.

71. The reaction mixture of claim 69, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate.

72. The reaction mixture of claim 70 or claim 71, wherein the sugar derivative substrate is selected from the group consisting of: glucaric acid and salts and lactones thereof; galactaric acid and salts and lactones thereof; and mannaric acid and salts and lactone thereof; or a mixture thereof.

73. The reaction mixture of claim 72, wherein the sugar derivative substrate is selected from the group consisting of glucaric acid, glucaric acid dilactone, 1,4-glucaric acid monolactone, 3,6-glucaric acid monolactone, sodium glucarate, potassium glucarate, calcium glucarate, galactaric acid, 1,4-galactaric acid monolactone, 3,6-galactaric acid monolactone, sodium galctarate, potassium galactarate, calcium galactarate, mannaric acid, mannaric acid dilactone, 1,4-mannaric acid monolactone, 3,6-mannaric acid monolactone, sodium mannarate, potassium mannarate, calcium mannarate, or a mixture thereof.

74. The reaction mixture of claim 73, wherein the sugar derivative substrate is glucaric acid, or a salt or lactone thereof.

75. The reaction mixture of claim 73, wherein the sugar derivative substrate is galactaric acid, or a salt or lactone thereof.

76. The reaction mixture of claim 73, wherein the sugar derivative substrate is mannaric acid, or a salt or lactone thereof.

77. The reaction mixture of claim 73, wherein the sugar derivative substrate is glucaric acid dilactone.

78. The reaction mixture of claim 73, wherein the sugar derivative substrate is mannaric acid dilactone.

79. The process of claim 73, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate comprising glucaric acid dilactone and mannaric acid dilactone.

80. The process of claim 73, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate consisting of glucaric acid dilactone and mannaric acid dilactone.

81. The process of claim 73, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate comprising glucaric acid dilactone, mannaric acid dilactone, and galactaric acid.

82. The process of claim 73, wherein the sugar derivative substrate is a heterogeneous sugar derivative substrate consisting of glucaric acid dilactone, mannaric acid dilactone, and galactaric acid.

83. The reaction mixture of any one of claims 69 to 82, wherein the mixture further comprises FDCA.

84. The reaction mixture of any one of claims 69 to 83, wherein the concentration of sugar derivative substrate in the mixture ranges from between 0.05-10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or within a range defined by any two of the aforementioned concentrations.

85. The reaction mixture of and one of claims 69 to 84, wherein the water- miscible organic solvent is selected from the group consisting of 1,4-dioxane, tetrahydrofuran, sulfolane, a glyme, N-methyl-2-pyrrolidone, methyl ethyl ketone, dimethyl formamide, and dimethyl sulfoxide.

86. The reaction mixture of claim 85, wherein the water-miscible organic solvent is 1,4-dioxane or sulfolane.

87. The reaction mixture of any one of claims 69 to 86, wherein the Bronsted acid is selected from the group consisting of hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, phosphoric acid, methanesulfonic acid, p-toluenesulfonic acid, benzenesulfonic acid, trifluoromethanesulfonic acid, acetic acid, and trifluoracetic acid.

88. The reaction mixture of claim 87, wherein the concentration of the Bronsted acid in the mixture ranges from between 0.05-10.0 M, 0.10-5.0 M, 0.2-4.0 M, or 0.4-3.0 M, or within a range defined by any two of the aforementioned concentrations.

89. The reaction mixture of any one of claims 69 to 88, wherein the halide salt is a metal halide or a tetraalkylammonium halide.

90. The reaction mixture of claim 89, wherein the metal halide is selected from the group consisting of FeBr₂, FeBr₃, FeCl₂, FeCl₃, CuBr, CuBr₂, CuCl, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, NaCl, NaBr, Nal, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, MgBr₂, KC1, KBr, and KI.

91. The reaction mixture of claim 65, wherein the metal halide is selected from the group consisting of FeBr₂, FeCl₂, CuBr₂, CuCl₂, ZnCl₂, ZnBr₂, NiCl₂, NiBr₂, LiBr, LiCl, CaCl₂, CaBr₂, MgCl₂, and MgBr₂.

92. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is CaBr₂ and the Bronsted acid is hydrobromic acid.

93. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is CaBr₂ and the Bronsted acid is hydrochloric acid.

94. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is CaBr₂ and the Bronsted acid is methanesulfonic acid.

95. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is CaBr₂ and the Bronsted acid is sulfuric acid.

96. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is MgBr₂ and the Bronsted acid is hydrobromic acid.

97. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is MgBr₂ and the Bronsted acid is methanesulfonic acid.

98. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is MgBr₂ and the Bronsted acid is sulfuric acid.

99. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is LiBr and the Bronsted acid is hydrobromic acid.

100. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is LiBr and the Bronsted acid is methanesulfonic acid.

101. The reaction mixture of any one of claims 69 to 90, wherein the metal halide salt is ZnCl₂ and the Bronsted acid is hydrochloric acid.

102. The reaction mixture of claim 89, wherein the tetraalkylammonium halide is selected from the group consisting of tetramethylammonium chloride, tetramethylammonium bromide, tetraethylammonium chloride, tetraethylammonium bromide, tetrabutylammonium chloride, and tetrabutylammonium bromide.

103. The reaction mixture of any one of claims 69 to 89 or 102, wherein the tetraalkylammonium halide salt is tetraethylammonium bromide and the Bronsted acid is methanesulfonic acid.

104. The reaction mixture of any one of claims 69 to 103, wherein the concentration of halide salt in the mixture ranges from between 0.01-3.0 M, 0.05-0.2 M, 0.1-1.0 M, or 0.2-0.5 M, or within a range defined by any two of the aforementioned concentrations.

105. The reaction mixture of claim 104, wherein the concentration of halide salt is at least 0.1 M.

106. The reaction mixture of claim 104 wherein the concentration of halide salt is less than 2.0 M, or less than 1.5 M, or less than 1 M, or less than 0.75 M, or less than 0.5 M but not zero.

107. The reaction mixture of any one of claims 69 to 106, wherein the mixture further comprises water.

108. The reaction mixture of claim 107, wherein the concentration of water in the mixture ranges from between 0.01-20.0 M, 0.01- 10.0 M, 0.1-5.0 M, or 0.2-1.0 M, or within a range defined by any two of the aforementioned concentrations.

109. The reaction mixture of any one of claims 69 to 108, wherein the mixture further comprises an alcohol.

110. The reaction mixture of claim 109, wherein the alcohol is selected from the group consisting of n-butanol, sec-butanol, isobutanol, 1-pentanol, 2-pentanol, 2-(2- chloroethoxy)ethanol), ethoxyethanol, and cyclohexanol.

111. The reaction mixture of claim 109 or claim 110, wherein the concentration of alcohol ranges from between 0.01-1.0 M, 0.1-l.OM, or 0.5-1.0M, or within a range defined by any two of the aforementioned concentrations.

112. The reaction mixture of any one of claims 69 to 111, wherein the mixture comprises compounds derived from the hydrolysis of cellulose, hemicellulose, or lignin.

113. The reaction mixture of any one of claims 69 to 112, wherein the mixture further comprises 2-furoic acid.