Patent Application
20230348352
The present application and disclosed embodiments relate to improved methods, reactants and reagents for synthesizing lactic acid. More specifically, the present application and disclosed embodiments relate to improved methods, reactants and reagents for synthesizing anhydrous lactic acid.
Lactic acid is a naturally occurring hydroxycarboxylic acid used in a variety of industries for a variety of applications. For example, lactic acid is used as a food additive, decontaminant and flavoring agent. Lactic acid is also a precursor for chemical and polymer synthesis of biodegradable and biocompatible polymers. In cosmetic and personal care products, lactic acid is used to moisturize skin, prevent acne and increase dermal collagen thickness. (Philipp, Babilas; Ulrich, Knie; Christoph, Abels, “Cosmetic and dermatologic use of alpha hydroxy acids” Journal of German Society of Dermatology, 10(7):488-49, 2012).
The global demand for lactic acid has increased steadily since 2013. In 2018, economic reports valued the global market for lactic acid at USD 2.64 billion and predicted an expected growth rate of 18.6% annually (CAGR) from 2019 to 2025. (Komesu, A., Oliveira, J. A. R. d., Martins, L. H. d. S., Wolf Maciel, M. R., and Maciel Filho, R., “Lactic acid production to purification: A review,” BioResources. 12(2). 4364-4383, 2017); see also (Grand View Research, “Lactic Acid Market Size, Share & Trend Analysis Report” Report ID: 978-1-68038-126-9, 2019).
Lactic acid is chiral molecule consisting of two enantiomers.: L-(+)-lactic acid or (S)-lactic acid and its mirror image D-(−)-lactic acid or (R)-lactic acid. In the pharmaceutical industry, the purity and chemical structure of reactants and reagents can drastically affect the resulting properties and therapeutic effectiveness of active pharmaceutical ingredients (APIs). There are very few suppliers for high quality lactic acid and specifically anhydrous lactic acid suitable in the manufacture of APIs. Most suppliers provide lactic acid in about 80%-95% solution with water (e.g., about 90% solution with water). Aqueous lactic acid contains significant impurities that are not suitable in the manufacture of APIs.
The primary methods of preparing L-lactic acid involve fermentation of carbohydrates followed by recovery and purification. Some of these methods are described in U.S. Pat. No. 2,232,554 and other published literature. (Borsook, H., Huffman, H. M. and Liu, Y.-P., J. Biol. Chem., “The Preparation of Crystalline Lactic Acid,” 102, 449, 1933). For example, a lactic acid solution can be produced by converting crude lactic acid into Ca-lactate by fermentation, crystallizing Ca-lactate, neutralizing Ca-lactate with mineral acid (sulfuric acid), and filtering to obtain a lactic acid solution. (Sidney Hsin-Huai Chow “Lactic Acid Review,” A Master's Thesis, 1957). Other methods of producing lactic acid involve fractional distillation of mixed ethers (ethyl and isopropyl ethers) in greater than 50% commercial syrup followed by crystallization. (Borsook, H., Huffman, H. M. and Liu, Y.-P., J. Biol. Chem., “The Preparation of Crystalline Lactic Acid,” 102, 449, 1933). These solvent extraction methods used to extract lactic acid from aqueous solution suffer from low efficiency. PCT/EP2015/067258 describes the conversion of crude lactic acid into a solid Mg-lactate followed by acidification with hydrochloric acid gas to produce a lactic acid solution from which lactic acid can be recovered by employing additional isolation and purification steps.
The preparation of anhydrous lactic acid often requires strenuous and complex post fermentation steps, which commonly include derivatization to Ca-/Zn-/NH4-salt, isolation of the respective salts, acid treatment of the salts, distillation, crystallization and additional isolation steps. One such method utilizes distillation at reduced pressure to obtain monomeric lactic acid, which is subjected to adiabatic crystallization to obtain dry lactic acid crystals. See e.g., U.S. Pat. No. 6,630,603; EP Patent No. 1317408; U.S. Patent Publication No. 2011/0319660.
There are no known and reliable processes available to isolate anhydrous lactic acid directly into non-aqueous solvents without involving aqueous lactic acid solution. There are also no known processes for the chemical synthesis of anhydrous lactic acid at industrial scales without employing a complex number of inefficient steps that ultimately result in an aqueous or low purity product. Therefore, improved methods for synthesizing anhydrous lactic acid are necessary to address the deficiencies in purity, complexity and yields of available conventional processes.
The present application and disclosed embodiments are directed to improved methods, reactants and reagents for synthesizing lactic acid on industrial scale for all applications. More specially, the present application and disclosed embodiments are directed to improved methods, reactants and reagents for synthesizing anhydrous lactic acid for pharmaceutical applications.
In an exemplary embodiment, a method of synthesizing anhydrous lactic acid is provided by reacting a compound of formula (Ia):
with an acid compound of formula HnX in a first solvent to produce a reaction mixture comprising a compound of formula (Ib) and a lactic acid compound of formula (I) in solution with the first solvent and/or water.
wherein each n is independently an integer other than 0, x is 0, or an integer other than 0, M is an alkali metal or alkaline earth metal and X is the conjugate base of the acid compound of formula HEX.
In an exemplary embodiment, the lactic acid compound of formula (I) is soluble in the first solvent, and the compound of formula (Ib) is insoluble in the first solvent. The resulting reaction mixture is filtered to produce a filtrate containing lactic acid in solution. The filtrate is crystalized from a second solvent to produce anhydrous lactic acid.
The foregoing and other objects, features and advantages of the present disclosure will become more readily apparent from the following detailed description of exemplary embodiments as disclosed herein.
Embodiments of the present application are described, by way of example only, with reference to the attached Figures, wherein:
The following examples and embodiments disclosed and described in this application are illustrative. Those of ordinary skill in the art will understand that various alterations to the embodiments may exist without departing from the scope or intent of the present application or exemplary embodiments disclosed, including variations with respect to the synthesis methods, processes, reactants, reagents, parameters and conditions described herein. The present application is directed to improved methods, reactants and reagents for synthesizing anhydrous lactic acid for use in industrial processes, including but not limited to, petrochemical processes; chemical and polymer synthesis; processes for the production of cosmetics and personal care products; processes for the production of food additives, decontaminants and flavoring agents; and processes for the production of pharmaceuticals and active pharmaceutical ingredients.
In an exemplary embodiment, an anhydrous lactic acid compound of formula (I) is produced by the synthesis and process steps depicted in
For the synthesis of anhydrous lactic acid depicted in
M is an alkali metal or alkaline earth metal. Suitable alkali metals and alkaline earth metals include, but are not limited to, calcium, sodium, potassium, magnesium, lithium, cesium, barium, beryllium or strontium. In an exemplary embodiment, M is calcium and the compound of formula (Ia) is calcium lactate hydrate. In another exemplary embodiment, the compound of formula (Ia) is calcium L-lactate pentahydrate.
HnX is an acid. Suitable mineral acids include, but are not limited to, sulfuric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, perchloric acid, chloric acid, hydrofluoric acid and nitric acid. Suitable organic acids include, but are not limited to, malonic acid, glutaric acid, citric acid, malic acid, tartaric acid, oxalic acid or formic acid. In an exemplary embodiment, the acid is sulfuric acid or oxalic acid.
X is the conjugate base of the acid used in the synthesis of
In an exemplary step of the synthesis of
The first solvent can be one or more ester solvents, including but not limited to, methyl acetate, ethyl acetate, isopropyl acetate or n-propyl acetate. Other suitable solvents include acetone, toluene, acetonitrile, methyl tert-butyl ether (MTBE), isopropanol, ethanol, methanol, tetrahydrofuran, butanol, butyl acetate, carbon tetrachloride, dichloroethane, dichloromethane, diethyl ether, diisopropyl ether, dimethyl sulfoxide, heptane hexane, methyl acetate, ethyl ketone, methyl tert-butyl ether, or methyl isobutyl ketone. The first solvent can be selected based on the ultimate use of final anhydrous lactic acid product. In exemplary embodiments, the first solvent is methyl acetate, ethyl acetate, isopropyl acetate and/or toluene.
The reaction of the compound of formula (Ia) with the acid compound of formula HnX in the first solvent produces a reaction mixture containing the compound of formula (Ib) and lactic acid (I) in solution with the first solvent and/or water.
Each n described herein is independently an integer other than 0. By way of example only, when the acid is HCl, n in HnX is 1; when the acid is sulfuric acid, n in HnX is 2. By way of example only, when calcium-lactate hydrate is used as Formula (Ia) reacting with HCl, n is 2 in Mn+, n is 1 in HnX, and n is 2 in
By way of example only, when calcium chloride is used in the compound of Formula (Ib) n is 2 in MXn. In some embodiments, each n in the equation above has the same value based on stoichiometry. The stoichiometry and/or the value for each n will be readily apparent to one of skill in the art.
In one exemplary embodiment, the compound of formula (Ib) is at least partially insoluble in the first solvent, and lactic acid (I) is at least partially soluble in the first solvent. In one exemplary embodiment, the compound of formula (Ib) is insoluble in the first solvent, and lactic acid (I) is soluble in the first solvent.
In the next step of the synthesis of
Suitable filtration techniques include vacuum filtration, gravity filtration, cold filtration, hot filtration, Nutsche agitated filtration, centrifuge filtration and robo-filtration. In an exemplary embodiment, gravity filtration is performed using a Buchner funnel. In another exemplary embodiment, gravity filtration is performed using a Hirsch funnel. The Buchner funnel and Hirsch funnel can be equipped with filter paper and cloth to facilitate the filtration.
In an exemplary embodiment after the first filtration, the first filtrate containing lactic acid in solution with the first solvent and/or water can be distilled to remove water and/or the first solvent and concentrate the lactic acid in the first filtrate. Maximizing the removal of the first solvent and water from the first filtrate by distillation maximizes the yield of anhydrous lactic acid.
After the initial filtration and distillation steps, the first filtrate containing lactic acid (I) can be isolated and subsequently crystallized by combining the lactic acid (I) with a second crystallization solvent and cooling the solution to create purified crystals of anhydrous L-lactic acid (I). Optionally, seed crystals of lactic acid can be added to the solution to initiate and accelerate crystallization.
To maximize recovery and yield of the end-product, lactic acid is only partially soluble in the second crystallization solvent. The second crystallization solvent can be one or more solvents including but not limited to toluene and heptane. Additional filtration steps can be employed to isolate and purify the resulting anhydrous lactic acid product.
Other processing steps can be employed after the first filtration step to increase the yield of anhydrous lactic acid. For example, residual water can be removed from the isolated first filtrate by azeotropically removing the water to produce anhydrous lactic acid. In an exemplary embodiment, azeotropic removal can be achieved by azeotropic distillation. A distillation solvent, such as toluene can be used to create an azeotrope with water to effect azeotropic distillation. In an exemplary embodiment, a Dean-Stark water trap can be used to azeotropically remove water from the isolated first filtrate containing lactic acid in solution to produce a dry/anhydrous lactic acid.
The degree of crystallization and purification of anhydrous lactic acid obtained from the solution containing crystallization solvent and lactic acid is heavily dependent on the water content of the filtrate and elimination of water from the first filtrate produced after initial filtration. In addition to the exemplary steps of synthesis disclosed herein, water content of the filtrate can be monitored using Karl Fischer titration and residual water can be azeotropically removed as described herein to increase yield and purity of the anhydrous lactic acid product. In an exemplary embodiment, water can also be removed by drying the filtrate over a drying agent, such as anhydrous Na2SO4. Molecular sieves and drying ovens can also be used to remove water from the first filtrate.
The exemplary methods of synthesizing anhydrous lactic acid disclosed herein can produce an anhydrous lactic acid product with less than 0.10% by weight water and less than 1% by weight polylactate impurities, such as lactide, oligomers of lactic acid and mixtures thereof. In some embodiments, the resulting anhydrous lactic acid is essentially free of water and free of polylactic acid and can be used in high precision, high purity industrial processes, such as the production of APIs. The resulting anhydrous lactic acid is substantially free of water and substantially free of polylactic acid and can be used in high precision, high purity industrial processes, such as the production of APIs. As used herein “substantially free of water and substantially free of polylactic acid” means that the product has less than about 5%, about 4%, about 3%, about 2%, about 1% or about 0.5% of water and/or polylactic acid.
In an exemplary embodiment of the synthesis of anhydrous lactic acid depicted in
The calcium lactate hydrate used in Reaction Scheme 1 and methyl acetate (MeOAc) was selected as a solvent based on the ultimate use of the anhydrous lactic acid end-product in the synthesis of an active pharmaceutical ingredient (API). After reacting calcium lactate hydrate with concentrated sulfuric acid in methyl acetate, the resulting slurry containing lactic acid can be filtered and concentrated. Residual water can be removed by absorption with calcium sulfate and additionally with azeotropic removal of residual water using vacuum distillation, including rotary evaporators or direct vacuum distillation, to produce an anhydrous lactic acid end-product.
In an exemplary embodiment of the synthesis of anhydrous lactic acid of
After reacting calcium lactate hydrate with hydrochloric acid, the calcium chloride produced forms a hydrated insoluble in MeOAc, which can be filtered off. The filtrate containing lactic acid can be further processed by isolating, recovering, filtering, concentrating, decanting distilling, crystallizing and/or dehydrating the filtrate to produce high purity anhydrous lactic acid.
In an exemplary embodiment of the synthesis of anhydrous lactic acid of
Calcium lactate hydrate can be neutralized with oxalic acid, which has pKa less than the pKa of lactic acid. Reaction Scheme 3 utilizes a slurry to slurry reaction in methyl acetate. Calcium oxalate is insoluble in methyl acetate and can be filtered off to create a pure lactic acid filtrate. The pure lactic acid filtrate can be further processed by isolating, recovering, filtering, concentrating, decanting, distilling, crystallizing and/or dehydrating the filtrate to produce high purity anhydrous lactic acid.
The anhydrous lactic acid end-product produced by Reaction Schemes 1-3 can be used to produce the API compound of formula (XXIII) by reacting the compound of formula (XXII), i.e., 1-{6-[(4-fluorophenyl)methyl]-5-(hydroxymethyl)-3,3-dimethyl-1H,2H,3H-pyrrolo[3,2-b]pyridin-1-yl}-2-[(2R,5R)-5-methyl-2-{[(3R)-3-methylmorpholin-4-yl]methyl}piperazin-1-yl]ethan-1-one (IUPAC name) or 1-(6-(4-fluorobenzyl)-5-(hydroxymethyl)-3,3-dimethyl-2,3-dihydro-1H-pyrrolo[3,2-b]pyridin-1-yl)-2-((2R,5R)-5-methyl-2-(((R)-3-methylmorpholino)methyl)piperazin-1-yl)ethan-1-one (name generated from ChemDraw Professional V. 17.1.0.105 (19), with anhydrous lactic acid in a solution of ethyl acetate as shown in the reaction step below.
Accordingly, provided herein is a method the preparation of a compound of Formula (XXIII):
the method comprising contacting a compound of Formula (XXII)
with the anhydrous lactic acid described herein to provide the compound of Formula (XXIII).
The examples below describe exemplary reaction conditions, parameters and reagents to carry out exemplary steps in the synthesis of anhydrous lactic acid. The following examples are illustrative of some of the embodiments described herein. Those of ordinary skill in the art will understand that various alterations to the examples may exist without departing from the scope or intent of the present application or exemplary embodiments disclosed, including variations with respect to the synthesis methods, processes, reactants, reagents, parameters and conditions described herein. The examples below can produce an anhydrous lactic acid product with less than 0.1% by weight water and less than 1% by weight polylactate impurities, such as lactide, oligomers of lactic acid and mixtures thereof. The examples can also be used to produce anhydrous lactic acid, and specifically L-(+)-lactic acid, D-(−)-lactic acid and DL-lactic acid.
The Examples described below may be used for preparation of high purity anhydrous lactic acid, including L-(+)-lactic acid, D-(−)-lactic acid and/or DL-lactic acid. The following examples are for the purpose of illustration only and are not meant to limit the scope of the embodiments and/or claims herein.
Chiral purity of the product was measured by an isocratic HPLC method using a chiral column with UV detection at 254 nm. The method was used for release testing of Calcium L-lactate to determine chiral purity and the content of Calcium D-lactate. The chemical structures of Calcium L-lactate and Calcium D-lactate are shown below.
The relative retention times (RRT) for D- and L-lactic acid using this method were as follows.
Integration and calculations were carried out by only integrating the peaks for L-lactic acid and D-lactic acid in the chromatograms.
% Calcium D-lactate=[AD-lactic acid/(AL-lactic acid+AD-lactic acid)]×100
Chiral purity (%)=100(%)−% Calcium D-lactate*
1HNMR data (including QNMR data) was obtained on a Varian Mercury 400 mHz machine.
In an exemplary embodiment of Reaction Scheme 1, concentrated H2SO4 (1.14 mL, 20.61 mmol, 0.9 eq.) was added drop wise to a cold (−14° C.) slurry of Ca-lactate hydrate (5 g, 22.9 mmol anhydrous basis, 1.0 eq.) and MeOAc (100 mL) in a flask under nitrogen. The slurry was stirred for 30 minutes at a temperature of −12° C. and for an additional 2 hours at room temperature. The resulting free flowing slurry was then filtered, and the filtrate was concentrated to produce 3.79 g (quantitative) of a viscous liquid. The filtrate of Example 1 can be further processed by isolating, recovering, filtering, concentrating, decanting, distilling, crystallizing and/or dehydrating the filtrate to produce anhydrous lactic acid.
In an exemplary embodiment of Reaction Scheme 1, concentrated H2SO4 (1.27 mmol, 22.9 mmol, 1.0 eq.) was added drop wise to a cold (−14° C.) slurry of Ca-lactate hydrate (10 g, 34.45 mmol 4H2O basis, 1.5 eq.) and MeOAc (100 mL) in a flask under nitrogen. The reaction mixture was stirred for 3 h at a temperature of −12° C. to −14° C. and for an additional 2 hours at room temperature. The resulting slurry was then filtered through a sintered funnel and concentrated on a rotatory evaporator to approximately 3 volumes. 5 volumes of heptane were then added slowly, which formed an oily immiscible bottom layer in the reaction mixture. The reaction mixture was then concentrated to 3 volumes. 5 volumes of heptane were added resulting in a similar bottom oily layer. The reaction mixture was then completely concentrated to a viscous oil, dissolved in 50 mL MeOAc and dried over anhydrous Na2SO4. The mixture was then concentrated to 2 volumes. 2 volumes of heptane were added followed by lactic acid seed crystals. Commercially purchased anhydrous lactic acid was used as seed in the initial experiment, and the material of Example 2 or commercially purchased anhydrous lactic acid was used as seed in later experiments. The reaction mixture was then cooled in an ice bath while stirring, resulting in a semisolid sludge with some white crystals. The semisolid sludge was then completely concentrated and subjected to high vacuum filtration to produce 3.57 grams of hygroscopic white solid anhydrous lactic acid. This synthesis yielded 86.5% by weight anhydrous lactic acid.
In an exemplary embodiment of Reaction Scheme 1, concentrated H2SO4 (3.06 mL, 55.12 mmol, 1.0 eq.) was added drop wise to a cold (−13° C.) slurry of Ca-lactate hydrate (20 g, 68.9 mmol based on 4H2O basis, 1.25 eq.) and MeOAc (200 mL) in a flask under nitrogen. The slurry was stirred for 3h at a temperature of −10° C. to −14° C. and for an additional 2 hours at room temperature. The free-flowing slurry was then filtered via a short pad of anhydrous Na2SO4 in a sintered funnel and concentrated on a rotary evaporator to approximately 2 volumes. The solution was then cooled to 0° C. followed by slowly adding 1.5 volume of heptane while stirring. At this point, L-lactic acid seed crystals and an additional 4.5 volumes of heptane (total 6 volume) were added. The resulting bilayer was then completely concentrated to a semisolid sludge. The semisolid was dissolved in 2 volumes of MeOAc, and 10 volumes of heptane were added slowly. An immiscible layer was formed at the bottom of the mixture. The mixture was then concentrated down to 2 volumes, and 10 volumes of heptane were added followed by additional seed crystals of lactic acid. A clumpy slurry was formed, which was completely concentrated to obtain white hygroscopic solid crystals of anhydrous L-lactic acid. The synthesis yielded 9.47 grams of 95.4% by weight anhydrous L-lactic acid.
In an exemplary embodiment of Reaction Scheme 1, concentrated H2SO4 (275.6 mmol, 1.0 eq.) was added drop wise over 15 minutes to a cold (−13° C.) slurry of Ca-lactate hydrate (100 g, 344.56 mmol based on 4H2O basis, 1.25 eq.) and MeOAc (800 mL) in a flask under nitrogen. The slurry was stirred for 6h at a temperature of −12° C. to −14° C. The slurry was then filtered via a Buchner funnel equipped with filter paper and cloth. The filter cake was washed with MeOAc (50 mL×2) and the total volume of 1000 mL of filtrate was produced. The filtrate was then divided into following fractions by measuring in a measuring cylinder:
The filtrate in aqueous solution of Fraction A was concentrated down to 30 mL, cooled with an ice bath to a temperature of 0 to 5° C., and 60 mL heptane was added drop wise to form an oily immiscible layer. At this point, 30 mg of anhydrous lactic acid crystals were added which immediately dissolved. The whole solution was then concentrated down to 30 mL. 60 mL of heptane was added and concentrated down to 30 mL and repeated 3 times. 60 mL of heptane was then added, cooled in an ice bath followed by the addition of 30 mg anhydrous lactic acid as seed crystals to form a slurry. The slurry was not free flowing or filterable. The slurry was again completely concentrated in a rotary evaporator, dissolved in 10 mL MeOAc, cooled in an ice bath followed by the addition of seed crystals and 60 mL of heptane to produce a slurry with better properties for filtering. The slurry was then completely concentrated to get white solid of anhydrous L-lactic acid sticking on the wall. The synthesis resulted in 12.2 grams of 82% by weight of anhydrous L-lactic acid.
The filtrate in aqueous solution of Fraction B was concentrated down to 30 mL, cooled in an ice bath to a temperature of 0 to 5° C. followed by a drop wise addition of 60 mL of toluene over 15 minutes. An oil immiscible layer was formed after the 60 mL of toluene was added. The bilayer was then concentrated down to 30 mL. To this solution, 60 mL toluene was added and concentrated down to 30 mL at 30° C. and repeated 3 times. Finally, 60 mL of toluene was added, the solution was cooled in an ice bath to a temperature of 0 to 5° C., followed by the addition of 30 mg anhydrous lactic acid seed crystals. The solution rapidly formed free-floating crystals with big chunks of anhydrous lactic acid. The solution was stirred until the big chunks of anhydrous lactic acid were broken and became a free-flowing filterable slurry. The slurry was then filtered under nitrogen to produce white crystals of anhydrous lactic acid. The synthesis formed 11.6 grams of 78% by weight anhydrous lactic acid.
The filtrate in aqueous solution of Fraction C was completely concentrated to a viscous liquid, which was divided into two parts of 6 g each in 15 mL centrifuge tubes. 600 μL H2O was then added to both to make approximately 90% aqueous solutions. The solutions were then cooled to 15° C., and anhydrous lactic acid seed crystals were added. The seeds dissolved at this temperature. The solutions were then gradually cooled to 10° C. and additional anhydrous lactic acid seed crystals were added, resulting in a slurry. The slurry was left in a fridge at a temperature of 6° C., and the seeds grew to bigger crystals. The slurry was then centrifuged at a temperature of 5° C. and 3000 rpm for 15 minutes. The resulting solid with crystals was then collected by decantation and dried in a vacuum oven at room temperature. A total of 3.9 g (29% yield) of solid was collected. The crystals were hard to transfer and dry relative to Fractions B-C. The supernatant liquid present in the wet crystals was azeotroped with toluene (20 mL×4). The resulting bilayer suspension with 20 mL toluene was cooled to a temperature of 0° C. followed by the addition of lactic acid seed crystals. A slurry was formed, which was distilled with 20 mL toluene two times. The resulting free flowing slurry was filtered under nitrogen to obtain 9.1 grams of 61% by weight anhydrous lactic acid in the form of white crystals.
In an exemplary embodiment of Reaction Scheme 1, concentrated H2SO4 (15 mL, 275.6 mmol, 1.0 eq.) was added drop wise for 30 minutes to a cold (−15° C.) slurry of Ca-lactate hydrate (100 g, 344.56 mmol based on 4H2O basis, 1.25 eq.) and MeOAc (800 mL) in a flask under nitrogen. The slurry was stirred for 6 hours at a temperature of −12° C. to −14° C. The slurry was then filtered via a Buchner funnel equipped with filter paper and cloth. The filter cake was washed with 100 mL MeOAc. The filtrate was concentrated to 300 mL. 200 mL of toluene was added, and the slurry was concentrated to 300 mL at a temperature of 30° C. This step was repeated 3 times. The resulting bilayer was cooled in an ice bath to a temperature of 4° C. and centrifuged at 400 rpm as anhydrous lactic acid crystals (50 mg) were added as seed. A solid was immediately formed with chunks. The suspension was stirred at room temperature for 15 hours. A sticky slurry was formed that was not free-flowing or filterable. 2 volumes of MeOAc were added to dissolve all solids, and the solution was concentrated on a rotary evaporator until it became a viscous oil. 1 volume of MeOAc and 2 volumes of toluene were added to the solution and concentrated down to 2 volumes. 2 additional volumes of toluene were added and concentrated down to 3 volumes. A free-flowing slurry was formed at this point, which was filtered under vacuum and dried under high vacuum for 4 hours to produce 37.2 grams of 75% by weight anhydrous lactic acid in the form of a white crystalline solid. The water content of the anhydrous lactic acid product was 0.562% by weight as determined by Karl Fischer titration.
In an exemplary embodiment of Reaction Scheme 1, concentrated H2SO4 (15.0 mL, 275.6 mmol, 1.0 eq.) was added drop wise over 30 minutes to a cold (−13° C.) slurry of Ca-lactate hydrate (100 g, 344.56 mmol based on 4H2O basis, 1.25 eq.) and MeOAc (800 mL) in a flask under nitrogen. The slurry was stirred for 6 hours at a temperature of −10° C. to −12° C. The slurry was then filtered via a Buchner funnel equipped with filter paper and cloth. The filter cake was washed with 100 mL MeOAc. The filtrate was concentrated to 100 mL. 200 mL of MeOAc was added and concentrated down to 100 mL and this was repeated. 200 mL of toluene was added, concentrated to 300 mL at a temperature of 30° C. and repeated 3 times. 200 mL of toluene was added. The resulting bilayer was stirred at room temperature and anhydrous lactic acid crystals (50 mg) were added as seed crystals. A sludge-like slurry was formed that was not free-flowing or filterable. The slurry was concentrated to 100 mL at a temperature of 30° C. 200 mL of toluene was added, concentrated down to 100 mL and this was repeated 2 times. A free-flowing slurry was formed at this point, which was filtered under vacuum and dried under high vacuum at room temperature for 24 hours to obtain 40.8 grams of 82% by weight anhydrous lactic acid in the form of a white crystalline solid.
Reaction Scheme 1 and the utilization of sulfuric acid produced high grade, high purity and high yields of anhydrous lactic acid from a slurry of Ca-lactate hydrate. The slurries produced by Reaction Scheme 1 were readily filtered and lactic acid was isolated in a purified end-product with high yields. Exemplary Reaction Scheme 1 can produce high purity and high yields of anhydrous lactic acid.
In an exemplary embodiment of Reaction Scheme 3, solid anhydrous oxalic acid (1.39 g, 15.5 mmol, 0.9 eq.) was added to a cold (−10° C.) slurry of calcium-L lactate hydrate (5 g, 1.0 equivalent, x mmol based on 4H2O) in MeOAc (100 mL). The resulting slurry was stirred for 40 minutes at a temperature of −10° C. followed by stirring for 46 hours at room temperature. The slurry was then filtered through a sintered funnel and concentrated on a rotary evaporator to produce 2.63 g of 94% by weight of lactic acid in the form of a thick viscous liquid. The filtrate containing lactic acid can be further processed by isolating, recovering, filtering, concentrating, decanting distilling, crystallizing and/or dehydrating the filtrate to produce high purity anhydrous lactic acid.
In an exemplary embodiment of Reaction Scheme 3, solid anhydrous oxalic acid (2.48 g, 27.54 mmol, 0.8 eq.) was added to a cold (−10° C.) slurry of calcium-L-lactate hydrate (10 g, 1.0 equivalent, 17.22 mmol based on 4H2O) in MeOAc (200 mL). The resulting slurry was warmed to room temperature and stirred for 18 hours at room temperature. The slurry was then filtered through a sintered funnel and concentrated on a rotary evaporator to 5 volumes to produce a filtrate. 5 volumes of heptane followed by lactic acid seed crystals were added to the filtrate. A sludge was formed, which was completely concentrated and kept in high vacuum to produce 3.86 g of 79% by weight anhydrous L-lactic acid in the form of a white crystalline solid.
Exemplary Reaction Scheme 3 can produce high yields of high purity anhydrous lactic acid, including L-(+)-lactic acid, D-(−)-lactic acid and/or DL-lactic acid.
The exemplary large-scale Synthesis Route (II) can be utilized to produce anhydrous L-lactic acid with less than 0.10% by weight water and less than 1% by weight of polylactate impurities, such as lactide, oligomers of lactic acid and mixtures thereof.
The equipment used in
Typical reactants, solvents and materials for conducting Synthesis Route II are outlined in Table 1.
In Synthesis Route II, before charging reactor 1 with the reactants, the oxygen content in the reactor is reduced to ≤ to 1% (by volume). In an exemplary embodiment, the oxygen content in reactor is 0.7% prior to initiating the reaction.
Reactor 1 is charged with 34.7 kg of isopropyl acetate and the stirring apparatus is started. The reactor was then charged with 7.5 kg anhydrous calcium L-lactate. The reaction mixture is maintained at a temperature of 0-10° C. In an exemplary embodiment, the reaction mixture is cooled and maintained at 7.3° C.
The reactor is then charged with 2.8 kg of sulfuric acid at a temperature of 0-10° C. The reaction temperature is maintained at 0-10° C. during the reaction. After 3 hours, a sample of the mixture is analyzed every 1-4 hours using 1H-NMR spectroscopy until assay by QNMR1 is greater than or equal to 11.5 or the difference between two consecutive samples is ≤0.5%.
In an exemplary embodiment the reaction is carried out for 7 h 10 min, the assay by QNMR1 yielded 8.8%, the assay by QNMR2 yielded 8.5% and the difference between two consecutive samples was 0.3%. The peak area of the lactic acid peak at 4.07 ppm was monitored for the quantitative NMR analysis. QNMR stands for quantitative 1HNMR where the amount of the test material was quantified (assayed) against an internal reference standard. In this case the internal reference standard was 1,3,5-trimethoxybenzene.
The reaction mixture is then filtered in a first filtration with a filter flask and a filter cake is generated. Vacuum filtration can be employed.
Reactor 1 is charged a second time with 13.9 kg of isopropyl acetate at a temperature of 0-30° C. In an exemplary embodiment, reactor 1 is charged a second time with isopropyl acetate at a temperature between 3.7-6.4° C. The isopropyl acetate is cooled to a temperature between 0-10° C. In an exemplary embodiment, the mixture is cooled to a temperature of between 6.3° C.
The filter cake from the first filtration was added to reactor 1 at a temperature of 1-10° C. In an exemplary embodiment, the filter cake was added to reactor 1 at a temperature of 6.3-6.4° C. The reaction mixture is stirred for 1-2 h at a temperature of 0-10° C. In an exemplary embodiment, the reaction mixture is stirred for 1 h 3 min at a temperature of 6.4-8.7° C.
The reaction mixture is filtered in a second filtration with a filter flask. The filtrate from the first filtration and the filtrate from the second filtration are added to reactor 2 through capsule filter in portions.
The mixture in reactor 2 is concentrated to ≤ to 45° C. under reduced pressure (P≤−0.08 MPa) until 0.5-1.0 volume is left. In an exemplary embodiment, the mixture is concentrated at a temperature of 16.5-32° C. and a pressure of −0.08 MPa.
Reactor 2 is additionally charged with 6.9 kg of isopropyl acetate and was stirred until fully dissolved. The mixture was sampled using Karl Fisher titration to determine water content. The mixture is cooled to a temperature of 20-25° C. In an exemplary embodiment, the mixture is cooled to a temperature of 24.3° C.
Anhydrous L-lactic acid seed crystals are added to the mixture. In an exemplary embodiment, 30.0 g of anhydrous L-lactic acid seed crystals are added to the mixture at a temperature of 20-25° C. for 1-2 h. The mixture is stirred at a temperature of 20-25° C. for 1-2 h. In an exemplary embodiment, the mixture is stirred at a temperature of 21.4-24.2° C. for 1-2 h.
The mixture is cooled to a temperature of 0-10° C. In an exemplary embodiment, the mixture is cooled to a temperature of 9.5° C. The mixture is stirred at a temperature of 0-10° C. for 1-2 h. In an exemplary embodiment, the mixture is stirred at a temperature of 2.3-9.5° C.
At a temperature of 0-10° C., toluene is added to the mixture through capsule filter. In an exemplary embodiment 52.2 kg of toluene is added to the mixture through capsule filter at a temperature of 0-10° C.
The mixture is stirred at a temperature of 0-10° C. for 2-3 h. In an exemplary embodiment, the mixture is stirred at a temperature of 1-2.8° C. for 2-3 h.
The mixture was filtered with a filter flask. The filter cake was rinsed with 6.3 kg of toluene twice. The solid from the filter is placed in a tray dryer and dried at 15-25° C. for 12 h. In an exemplary embodiment, the drying temperature is 20-21° C. The solid is sampled for residual solvent analysis every 4-12 h until residual isopropyl acetate is ≤5000 ppm and the residual toluene is ≤890 ppm. In an exemplary embodiment, the product contained 563 ppm isopropyl acetate and 277 ppm toluene.
The resulting product is an anhydrous L-lactic acid. In an exemplary embodiment, the resulting product is 6.0 kg of 99.3% by weight anhydrous L-lactic acid (based on 1H-NMR spectroscopy). The yield of Synthesis Route II is at least 47% and has a chiral purity of 100%.
Reaction scale and yield for two batches of anhydrous L-lactic acid produced by Synthesis Route II are provided in Table 2.
1HNMR
Tables 3 and 4 summarize the chemical properties of the anhydrous lactic acid end products of Batches 1 and 2.
The exemplary synthesis and reaction schemes disclosed herein can be used to produce anhydrous lactic acid, and specifically L-(+)-lactic acid, D-(−)-lactic acid and DL-Lactic acid for use in industrial processes, including but not limited to petrochemical processes; chemical and polymer synthesis; processes for the production of cosmetics and personal care products; processes for the production of food additives, decontaminants and flavoring agents; and processes for the production of pharmaceuticals and active pharmaceutical ingredients.
The present application claims priority under 35 U.S.C. § 119(e) to U.S. Provisional Application No. 63/019,870 filed on May 4, 2020, which is hereby incorporated by reference in its entirety.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2021/030457 | 5/3/2021 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 63019870 | May 2020 | US |
