Method for producing L-threonate from L-xylonic acid

Abstract

An efficient method for producing L-threonic acid from L-xylonic acid is disclosed.

Description

[Technical Field]

[0001] The present disclosure relates to a process for producing high-purity L-threonate from L-xylonic acid, comprising providing L-xylonic acid, decarboxylating the L-xylonic acid to produce L-threose, and oxidizing the L-threose to produce L-threonate. The disclosure also relates to recycling unreacted materials within the process. [Background technology]

[0002] L-threonic acid is a valuable commercial sugar acid, and its salts are used in pharmaceutical and supplement preparations. Magnesium L-threonate and calcium L-threonate, in particular, are important products in the supplement industry. Salts of L-threonic acid have traditionally been produced from ascorbic acid by alkaline decomposition or peroxide decarboxylation, as disclosed in U.S. Pat. Nos. 4,822,816, 4,968,716, and Chinese Patents Nos. 1,267,662A and 106,083,567A. However, these methods use expensive reagents, have low selectivity, and are performed in dilute solutions. Therefore, there remains a need for selective production of high-purity L-threonate salts from readily available raw materials. Summary of the Invention

[0003] A process for the preparation of L-threonate has been found, which is the subject of the present invention, and is characterized in that it comprises the following steps: L-xylonic acid is provided and decarboxylated to give L-threose, and L-threose is oxidized to L-threonic acid, preferably using a noble metal catalyst and more preferably after removing unreacted acid. In order to minimize waste and reduce operating costs, the process preferably comprises the following recycling step: separation of unreacted L-xylonic acid from L-threose and reuse as raw material for L-threose production, preferably elution of the reaction product through a separation zone containing a cation exchange resin. DETAILED DESCRIPTION OF THE INVENTION

[0004] definition As used herein, the term L-xylonic acid refers to an aldonic acid is This refers to L-xylonic acid and its salts. Salts of L-xylonic acid are called L-xylonates. For example, the sodium salt of L-xylonic acid is sodium L-xylonate.

[0005] As used herein, the term L-threose refers to L-threose, which is a rare sugar and is not currently produced industrially.

[0006] As used herein, the term KLG refers to 2-keto-L-gulonic acid and its salts. Salts of 2-keto-L-gulonic acid are called 2-keto-L-gulonates. For example, the sodium salt of 2-keto-L-gulonic acid is sodium 2-keto-L-gulonate. KLG is an intermediate in the production of ascorbic acid.

[0007] As used herein, the term L-sorbose refers to the ketose L-sorbose, which is an intermediate in the production of ascorbic acid.

[0008] As used herein, the term metal hydroxide refers to hydroxide salts of sodium, potassium, lithium, magnesium, or calcium.

[0009] As used herein, the term "decarboxylation" refers to the removal of a carboxyl group (-COOH) by a chemical reaction or physical process. Typical products of a decarboxylation reaction may include carbon dioxide (CO) or formic acid.

[0010] The term "electrochemistry" refers to chemical reactions that take place at the interface between an electrical conductor (electrode) and an ionic conductor (electrolyte). Electrochemical reactions can generate an electrical potential between two conductive materials (or two portions of a single conductive material) or can be induced by the application of an external voltage. In general, electrochemistry deals with situations where oxidation and reduction reactions are separated in space.

[0011] As used herein, the term "electrolysis" refers to an electrochemical oxidation or reduction reaction that results in the breaking of one or more chemical bonds. As used herein, electrolytic reactions preferably describe reactions that occur as a product of interaction with a cathode or an anode.

[0012] Providing L-xylonic acid This method requires providing L-xylonic acid as a raw material for the production of L-threonic acid. L-xylonic acid can be produced by different routes, for example, through the oxidation of L-sorbose, as in Isbell et al., J. Res. Nat. Bur. Stand. 29 (1942) 227-232 and U.S. Patent No. 6,894,199 B2. KLG can be decarboxylated using alkaline hydrogen peroxide to produce xylonic acid in good yield, as in Isbell et al., Carbohydr. Res. 36 (1974) 283-291 and U.S. Patent No. 6,894,199 B2. L-xylose, like all aldoses, can be oxidized to its corresponding aldonic acid, L-xylonic acid, via a noble metal catalyst. KLG can also be electrochemically decarboxylated to produce L-xylonic acid.

[0013] Xylonic acid decarboxylation Aldonic acids can be decarboxylated using various chemical systems, including hypochlorous acid and hydrogen peroxide systems, as in U.S. Patent No. 5,714,602. Aldonic acids can be selectively decarboxylated to yield sugars with one less carbon using an electrochemical cell, as in U.S. Patent Nos. 7,598,374, 7,955,489, and 9,702,047. For example, U.S. Patent No. 7,955,489 describes the electrolytic decarboxylation of aqueous D- or L-arabinonic acids to yield erythrose. Electrochemical decarboxylation of sugar acids is a two-electron oxidation.

[0014] In one embodiment of the present disclosure, the decarboxylation of xylonic acid is carried out using an electrochemical cell. Preferably, the electrochemical cell includes an anode, a cathode, and a cation exchange membrane separating the anode and cathode compartments. In one embodiment, L-xylonic acid is provided in the cell by simultaneous electrochemical decarboxylation of KLG.

[0015] L-threose oxidation Aldoses can be selectively oxidized to aldonic acid salts by chemical oxidation. Noble metal catalysts have been widely described in the literature, and gold catalysts in particular have been shown to be very effective for this oxidation, as described by Theilecke, et al., Catalisalysis Today, 115-120 (2007). L-threose can be oxidized to magnesium L-threonate as described in PCT Application No. PCT / US2020 / 070085.

[0016] In one embodiment of the present disclosure, the L-threose oxidation step is carried out using pressurized oxygen or air in the presence of a metal hydroxide. Preferably, the oxidation is carried out using a gold-based catalyst. More preferably, more than 95% of the L-threose is converted to L-threonic acid.

[0017] Threose Refining Mixtures of sugars, sugar acids, and polyols are often separated by chromatography, and industrially, simulated moving bed chromatography is used. A separation zone containing a cation exchange resin can be used as the chromatography medium, and different cation species are used to produce different sugar elution rates. Calcium has been widely used to separate glucose and fructose, as well as galactose and tagatose, as in U.S. Patent Nos. 3,416,961, 4,472,203, and 8,802,843. Sodium has been used to separate glycerol and erythritol, as in U.S. Patent No. 6,030,820.

[0018] In one embodiment of the present disclosure, a solution of L-threose and L-xylonic acid produced from the electrochemical decarboxylation of L-xylonic acid is eluted through a separation zone containing a cation exchange resin. Water is the eluent, and two product solutions are collected, one consisting primarily of L-threose and the other consisting primarily of acid. The cation exchange resin is preferably in the same cationic form as the acid. [Example]

[0019] [Example 1] A 2 molar solution of xylonic acid was provided. This solution was used as the anolyte that flowed through an electrochemical cell containing a graphite foil anode, a cation exchange membrane, and a stainless steel cathode. The catholyte was a 3.5 molar solution of potassium hydroxide. The temperature of the anolyte was maintained at 31°C. A current of 90 mA / cm2 geometric electrode surface was applied to the cell. Neutralization of the anolyte was maintained by adding potassium hydroxide to the anolyte. The cell was run for 6.8 hours. At the end of the reaction, there were 932 mmol of L-xylonic acid and 694 mmol of L-threose.

[0020] [Example 2] A 2 molar solution of potassium 2-keto-L-gulonic acid was provided at a pH of 6. This solution was used as the anolyte, which flowed through an electrochemical cell equipped with a graphite foil anode, a cation exchange membrane, and a stainless steel cathode. The catholyte was a 3.5 molar solution of potassium hydroxide. The anolyte temperature was maintained at 45°C. A current of 100 mA / cm2 geometric electrode surface was applied to the cell. Neutralization of the anolyte was maintained by adding potassium hydroxide to the anolyte. The cell was run for 19.5 hours. At the end of the reaction, there were 5.4 mmol of KLG, 254 mmol of L-xylonic acid, and 577 mmol of L-threose.

[0021] [Example 3] 350 ml of a 50 gram per liter L-threose solution, provided from the electrochemical decarboxylation of KLG, was added to a 1 L stirred tank pressure vessel. 2.8 g of a 4.5% gold catalyst and 9.78 g of magnesium hydroxide were added to the solution. The vessel was purged once with oxygen, then pressurized to 100 psi with oxygen and stirred. The reaction was stopped after 3 hours. 98.6% of the L-threose was converted to magnesium L-threonate.

[0022] [Example 3] A 2-liter column was prepared and packed with Diaion UBK550 cation resin in potassium form and maintained at 70°C. 150 ml of a 25% Brix solution of L-threose and L-xylonic acid was obtained from the electrochemical decarboxylation and eluted with water at 0.54 bed volumes per hour. The % Brix of the elution was measured using refractive index. L-threose and L-xylonic acid were baseline dissolved, and the L-threose fraction was collected, from which 98% of the acid was removed.

[0023] statement

[0024] 1) A method for producing L-threonic acid from L-xylonic acid, comprising providing L-xylonic acid, decarboxylating the L-xylonic acid to L-threose, and oxidizing the L-threose to L-threonic acid.

[0025] 2) The method of statement 1, wherein L-xylonic acid is produced from chemical decarboxylation of L-sorbose or KLG.

[0026] 3) The method of statement 1, wherein L-xylonic acid is produced from the oxidation of L-xylose.

[0027] 4) The method of statement 1, wherein L-xylonic acid is decarboxylated to threose using hypochlorous acid or hydrogen peroxide.

[0028] 5) The method of statement 1, wherein L-xylonic acid is decarboxylated to threose in an electrochemical cell.

[0029] 6) The method according to statement 5, wherein L-xylonic acid is provided by simultaneous decarboxylation of KLG.

[0030] 7) The method of any one of statements 1-6, wherein L-threose is oxidized to L-threonic acid using a catalyst in the presence of oxygen and a metal hydroxide.

[0031] 8) The method of statement 7, wherein the catalyst is gold-based.

[0032] 9) The method of any one of statements 1-8, wherein threose is purified by eluting the decarbonated solution through a separation zone containing a cation exchange resin.

Claims

1. A method for producing L-threonic acid from L-xylonic acid, comprising: decarboxylating 2-keto-L-gulonic acid (KLG) to L-xylonic acid; decarboxylating the L-xylonic acid to L-threose; and oxidizing the L-threose to L-threonic acid. The decarboxylation of the 2-keto-L-gulonic acid (KLG) to L-xylonic acid and the decarboxylation of the L-xylonic acid to L-threose are carried out simultaneously in an electrochemical cell. method.

2. 2. The method of claim 1, wherein the L-threose is oxidized to L-threonic acid using a catalyst in the presence of oxygen and a metal hydroxide.

3. The method of claim 2 wherein the catalyst is gold-based.

4. 4. The method according to claim 1, wherein the L-threose is purified by eluting the decarboxylated solution through a separation zone containing a cation exchange resin.

5. The method of claim 2, wherein the metal hydroxide is selected from the group consisting of sodium hydroxide, potassium hydroxide, lithium hydroxide, magnesium hydroxide and calcium hydroxide.

6. The method of claim 3, wherein the metal hydroxide is selected from the group consisting of sodium hydroxide, potassium hydroxide, lithium hydroxide, magnesium hydroxide and calcium hydroxide.

7. The method of claim 2, wherein the oxygen is pressurized oxygen or air.

8. The method described in claim 3, wherein the oxygen is pressurized oxygen or air.

9. The method of claim 1, wherein more than 95% of the L-threose is converted to L-threonic acid.

10. The method of claim 2, wherein more than 95% of the L-threose is converted to L-threonic acid.

11. The method of claim 3, wherein more than 95% of the L-threose is converted to L-threonic acid.