GLUCOSAMINE SULFATE METAL CHLORIDE COMPOSITIONS AND PROCESSES OF PREPARATION THEREOF

Abstract: Glucosamine compositions comprising the compounds glucosamine sulfate metal chloride, wherein the metal, i.e., the cation is potassium, sodium, magnesium, zinc, lithium or manganese. The compounds have purity levels of at least about 97 %, with water present in a maximum amount of about 10 wt.%, based on the weight of the composition. The compounds are prepared by contacting glucosamine hydrochloride with the metal sulfate in the presence of water to form an aqueous solution of glucosamine sulfate metal chloride and thereafter freeze-drying the solution at a temperature and at a reduced pressure for such period of time that at least about 90 wt.% of the water is removed and decomposition of the compound glucosamine sulfate metal chloride is limited to a maximum of about 3 %.

Description: GLUCOSAMINE SULFATE METAL CHLORIDE COMPOSITIONS AND PROCESSES OF PREPARATION THEREOF Field of Invention The invention relates to glucosamine sulfate metal chloride compositions and processes for preparing same. The glucosamine sulfate metal chloride compositions of the invention are true compounds having a purity level of at least about 97%. Background of the Invention Glucosamine is a well known and widely used substance for the treatment of rheumatic fever, arthritic and arthosic complaints, in the acute as well as chronic forms, as well as in the treatment of pathological conditions originating jfrom metabolic disorders of the osteo-articular tissue. Although products in the marketplace are labeled as, or referred to as, "glucosamine sulfate" or "stabilized glucosamine sulfate," they are misnomers, since such products are not true compounds, but rather are unreacted mixtures of glucosamine hydrochloride and a salt such as potassium or sodium sulfate. Mixed salts of glucosamine hydrochloride and alkaline or earth alkaline metal sulfates such as potassium sulfate, and sodium sulfate are well known. Such mixed salts are used rather than glucosamine sulfate alone since the latter is unstable in view of its highly hygroscopic nature and the facility with which its amino group oxidizes if not completely saltified, see, e.g., U.S. Patent 4,642,340 and U.S. Patent 3,683,076 which discloses a mixture of glucosamine sulfate and glucosamine hydroiodide. Free glucosamine base may be prepared by the method recited in Chem. Ber.. volume 75, page 1274. Such method involves the treatment of glucosamine hydrochloride with an ethanolic solution of a tertiary base such as triethyl-amine. Triethylamine hydrochloride is filtered off and the free glucosamine is then recovered from the reaction mixture. However, triethylamine is a toxic material even in small quantities and the yield of the free glucosamine base is quite low. In EP 0214642, free glucosamine base is converted to a mixed salt of glucosamine sulfate and potassium chloride by dissolving the glucosamine base in water, adding a stoichiometric quantity of concentrated sulfuric acid to form a solution of glucosamine sulfate in water and dissolving a stoichiometric amount of potassium chloride in the solution. The mixed salt is precipitated from the solution by addition of a precipitant such as isopropanol, stirring the mixture for about 14 hours to complete the precipitation, cooling the reaction mass to 0°C and recovering the precipitated salt by filtration. This process results in low yields. Sfltnmw Of the Invention It has now been found possible to prepare compositions comprising true compounds of glucosamine sulfate metal chlorides, wherein the metal, i.e., the cation, is potassium, sodium, magnesium, zinc, lithium or manganese. The compounds will have a purity level of about 97%, preferably at least 99%. Moreover, the processes of the invention avoids the use of toxic reagents such as triethylamine and also avoids the use of precipitants such as isopropanol, thereby permitting substantially quantitative yields with little or no impurities present other than very minor quantities of water. Detailed Description of the Invention The invention pertains to novel compositions and processes for preparing same. The compositions comprise: (a) glucosamine sulfate metal chloride compounds having a purity level of at least about 97%, wherein the metal is selected from the group consisting of potassium, sodium, magnesium, zinc, lithium and manganese; and (b) water, present in a maximum amount of about 10 wt.%, based on the weight of the composition Preferably, the compounds will have purity levels of at least 99%. Indeed, the processes of the invention typically result in compounds having purity levels in excess of 99%. The principal impurity will be water which is preferably present in a maximum amount of 5 wt.%, based on the weight of the composition Typically, the processes of the invention will produce compositions with water contents of not greater than 3 wt.%. Any water present in the compositions of the invention is not to be regarded as an "impurity" in the classical sense. The compositions of the invention are intended to be ingested and minor adjustments in the dosage to be ingested can be readily made to account for such water. Prior art compositions referred to as glucosamine sulfate potassium chloride or glucosamine sulfate prepared using isopropanol or acetone as a precipitant exhibit unacceptable chloride assay values of about 93% and densities of 0.55-0.65, indicating that potassium chloride is abstracted from the composition and remains in the aqueous precipitant layer. The glucosamine sulfate metal chloride compounds of the invention have densities which vary depending on the particular metal chloride, and are set forth in the Examples below. The chloride assay value of the compounds of the invention remain about 100 wt.%, prior to and subsequent to nitrogen sparging, which indicates that true compounds, rather than mixtures of salts or mixtures of reacted components plus unreacted components have been prepared by the processes of the invention. Also as discussed below, a simple test involving the addition of the composition to a mixture of liquid halogenated aliphatic hydrocarbons with a density of about 2.0 g cc will readily verify whether a composition alleged to be stabilized glucosamine sulfate, i.e., glucosamine sulfate metal chloride, is a true compound or is a mixture of unreacted glucosamine hydrochloride and a metal sulfate. In the presence of the halogenated hydrocarbons, the true compound will float as a layer on the top, whereas some of the mixture of unreacted glucosamine hydrochloride and the metal sulfate will float on the top and some of such mixture will fall as a precipitate to the bottom. The processes for preparing the novel compositions of the invention are quite simple and straightforward and typically result in quantitative yields. The processes involves the following steps: (a) contacting glucosamine hydrochloride with a metal sulfate in the presence of water to form an aqueous solution of glucosamine sulfate metal chloride, wherein the metal is potassium, sodium, magnesium, zinc, lithium or manganese; and (b) recovering the compound glucosamine sulfate metal chloride by freeze- drying the solution from step (a) at a temperature and at a reduced pressure for such period of time that: (i) at least about 90 wt.% of the water is removed and (ii) decomposition of the compound is limited to a maximum of about 3 wt.%. Typically, the glucosamine hydrochloride and metal sulfate are contacted in stoichiometric quantities in the presence of sufficient water to form a concentration of solids of about 15 to 45 wt.%, preferably 20 to 35 wt.%, and the contacting, i.e., step (a), takes place for a period of about 15 minutes to 2 hours. Step (a) takes place at temperatures of about 20 to about 45 °C. Higher temperatures are undesirable since exposure to such higher temperatures for prolonged periods of time will lead to decomposition, as evidenced by a yellowing of the solution. The freeze-drying in step (b) is typically carried out at a pressure of not greater than about 800 milliTorr, preferably 300 to 500 milliTorr, and at a temperature of about -60°C to 0°C, preferably -40 to -5°C. The processes of the invention avoid the use of precipitants such as isopropanol, acetone, dioxane, etc. in order to recover the glucosamine sulfate metal chloride from the aqueous reaction mixture. It has also been found that if removal of the water by distillation is used to recover the glucosamine sulfate metal chloride, some decomposition of the product occurs, even if the distillation is carried out at moderate temperatures of about 50 °C and at a pressure of about 20 mm Hg. Decomposition of the product is evidenced by a yellowing of the product and a shift in taste from sweetish and slightly salty to a bitter taste. When the water is attempted to be removed under vacuum at a pressure of about 20 mm Hg at ambient temperatures, significant foaming of the reaction mass occurs which prevents the water from being distilled off without also causing the product to flow out of the flask containing the aqueous solution. The following examples serve to illustrate the embodiments of this invention Unless otherwise indicated to the contrary, all parts and percentages are on a weight basis. Kxymple 1 In this example, an attempt was made to isolate the product from an aqueous solution of glucosamine sulfate by removing the water by vacuum distillation. A one-liter, three-necked flask equipped with a thermometer, stirrer, heating mantle and condenser was charged with 352.7 g of purified water, 107.8 g (0.5 mole) of glucosamine hydrochloride. The glucosamine hydrochloride promptly went into solution, with stirring (the dissolution of the glucosamine hydrochloride was endothermic in nature). After stirring for a few minutes, 43.5 g (0.25 mole) of potassium sulfate was added to the solution and stirring was continued for about one hour at 35-40°C to complete the reaction. The clear solution was transferred to a one-liter single-neck flask and water was stripped off at 60-65 ° C under a vacuum of approximately 20 mm Hg. It was noticed that the product turned progressively yellow in color as the water was being stripped off. The product was dried under vacuum at 70 °C for 8 hours. The product assay, by titration, was 98.5%. The yield of product was 147.5 g (97.5% of theory). However, the product had a yellow-orange color and was therefore not deemed to be acceptable, notwithstanding that the assay and yield were good. E am le 7 The equipment described in Example 1 was employed in this example. 56 g (0.26 mole) of glucosamine hydrochloride and 200 ml of isopropanol were charged to the flask, resulting in a slurry. 25.2 g (0.25 mole) of triemylamine were added over a 1-hour period and stirring continued for 24 hours at 25 °C and thereafter filtered. Gas chromatographic analysis of the filtrate indicated the presence of free triethylamine which is a toxic material. Example 3 This example was carried out to demonstrate the process of the invention. Example 1 was repeated up to the point of obtaining the clear solution of glucosamine sulfate potassium chloride. The water was then stripped off from the clear solution by freeze- drying under the following conditions: The freeze temperature was set at -40°C, the condenser set point was -45 °C, the vacuum set point was 200.0 milliTorr and the vacuum safety was set at 800 milliTorr. The solution was then subjected to the following freeze- drying steps: Si£B Temp,°C Time r minutes 1 -30 120 2 -15 300 3 -5 540 4 0 540 5 10 300 6 20 240 Post Heat 25 60 A white powder was obtained in a yield of 98.5% of theoretical; the assay of die product was 100.3%. Example 4 This example was carried out to prepare glucosamine sulfate potassium chloride by the prior art method of precipitation using isopropanol. The same equipment as employed in Example 1 was used for this Example. 25.9 g (0.12 m) of glucosamine hydrochloride was added to 84 g of purified water in the flask and the mixture was stirred to obtain a clear solution. 10.6 g of potassium sulfate was added to the solution and stirring was continued for 1 hour at 25-30 °C. Thereafter, 336 g of isopropanol were added to precipitate the glucosamine sulfate potassiiun chloride. The reaction mixture was maintained at 20 °C for 4 hours and the product was recovered by filtration. The product was washed with 100 g of isopropanol and dried under vacuum. The yield was 31 g (85.4% of theoiy). The product was then assayed by titration and the assay result was 93%, which was not deemed to be acceptable. The results of this example indicate that precipitation of glucosamine sulfate potassium chloride is undesirable in several respects: low yield, poor volume efficiency, high solvent disposal cost, low product assay and the possibility of contamination of the final product with residual isopropanol. Example 5 This example was carried out to prepare glucosamine sulfate potassium chloride by the prior art method of precipitation using acetone. Example 4 was repeated using 336g of acetone to precipitate the product. The product yield was 32.6g (90% of theory). The product assayed by titration was 93.4% which was deemed to be unacceptable. F.xatnp1_> 6 The purpose of this example was to compare glucosamine sulfate potassium chloride obtained (a) by preparing a synthetic mixture of solid glucosamine hydrochloride and potassium sulfate; (b) from various commercial sources; and (c) from Examples 4 and 5 with that prepared by the freeze-dried process of the invention of Example 3. The synthetic mixture was prepared by thoroughly mixing (but not milling) 400 g of glucosamine hydrochloride with 160 g of potassium sulfate. The particular method by which the various commercial-sourced glucosamine sulfate potassium chloride samples were prepared was not known. However, based on the results set forth in Table I below, it appears that the commercial-sourced glucosamine sulfate potassium chloride was prepared by thoroughly mixing stoichiometric amounts of glucosamine hydrochloride and potassium sulfate. To demonstrate that the glucosamine sulfate potassium chloride of the invention differed from the synthetic salt mixture, samples of the two materials were subjected to X- RayDiffractionAnalysisusingaDexco8532/8806x-raydiffractometer. The samples were scanned from 5-65° 2Θ. The four most intense peaks are set forth below: Intensity GSPC * GSPC * Peak Freeze-Dried Svnthetic Mixture 100% Peak 7.396 5.210 2nd Peak 2.930 3.335 3rd Peak 3.919 7.340 4th Peak 3.688 3.745 * GSPC = Glucosamine Sulfate Potassium Chloride The comparison of the various materials was carried out using the following procedure: A 1-liter glass beaker was provided with a paper thimble of 12.1 cm in length and 4.4 cm in diameter. A glass tube with a fritted end having a length of 25.4 cm, an outer diameter of 7.6 mm and an inner diameter of 5.1 mm was inserted into the thimble such that the end thereof was approximately 5 mm from the bottom of the thimble. Glucosamine sulfate potassium chloride (50 g) from various sources was placed in the thimble and the open end of the glass tube was connected to a nitrogen gas cylinder. Nitrogen was sparged through the frit at the rate of 56.6 liters/minute for approximately 15 minutes and lighter material cascaded over the thimble and was collected in the beaker. The material in the thimble was measured for its density and assayed by titration for glucosamine hydrochloride prior to commencement of nitrogen sparging. The fraction sparged out was also measured for specific rotation and assayed. The fraction remaining in the thimble was also measured for specific rotation. Table I below indicates the results. TABLE I GSPC * Density Imtial Fraction Out Remaining Fraction Source Appearance g___ Assay $p r Rpt. Ass&y $p. Rot, Synth. White Mixture Crystals 1.20 98.6% 67.52 131.8% 26.80 White Fine Ex. 3 Powder 0.92 100.3% 50.90 100.1% 52.71 White Fluffy Ex. 4 Powder 0.58 93.0% 50.30 90.6% 50.23 White Fluffy Ex. 5 Powder 0.61 93.4% 53.49 95.5% 52.01 Comm'l White Fine A Powder 1.16 100.2% 62.10 118.0% 42.10 Comm'l White Fine B Powder 1.21 100.7% 62.65 119.7% 41.54 Comm'l White Cryst C Powder 1.22 100.4% 62.17 118.6% 42.03 Comm'l White D Crystals 1.15 106.7% 65.65 128.1% 28.60 GSPC * = Glucosamine Sulfate Potassium Chloride The following conclusions may be drawn from the results set forth in Table I: 1. Based on appearance and density, commercial samples A-D were identical compositions and, based on such factors, the commercial samples appeared to be of the same composition as the synthetic mixture. 2. For the synthetic mixtures and the commercial samples, the initial assays, i.e., before nitrogen sparging, were all satisfactory. However, after sparging, the assays obtained from the material sparged out of the thimble were considerably different from the initial assays indicating that the compositions were not true compounds. This was further reinforced by the different specific rotation values obtained in respect to the material sparged out versus those of the material remaining in the thimble. 3. The compositions ofExamples 4 and 5 obtained by isopropanol and acetone precipitants, had unacceptable initial assays and very low densities. These results indicate that some potassium chloride had been abstracted from the compositions and remained dissolved in the aqueous precipitant filtrate. Thus, although the initial assays were comparable to those of the materials sparged out tending to indicate that a compound rather than a mixture was present, such compound nevertheless had an unacceptably low purity level. 4. The Example 3 composition prepared by the process of the invention was a highly pure true compound in all respects, i.e. , density, initial assay, assay of the material being sparged out and comparable specific rotation values of the material sparged out and that remaining in the thimble. Example 7 Glucosamine sulfate sodium chloride was prepared by the following procedure. A one-liter, three-necked flask equipped with a thermometer, stirrer, heating mantle and condenser was charged with 1720 g of purified water and 431.5 g (2.0 moles) of glucosamine hydrochloride. The glucosamine hydrochloride promptly went into solution, with stirring (the dissolution of the glucosamine hydrochloride was endothermic in nature). After stirring for a few minutes, 142 g (1.0 mole) of sodium sulfate was added to the solution and stirring was continued for about one hour at 35-40 ° C to complete the reaction. The water was then stripped off from the resultant clear solution by freeze-drying under the following conditions: The freeze temperature was set at -40°C, the condenser set point was -45 °C, the vacuum set point was 200.0 milliTorr and the vacuum safety was set at 800 milliTorr. The solution was then subjected to the following freeze-drying steps: Step Temp.°C Time, minutes 1 -30 120 2 -15 300 3 -5 540 4 0 540 5 10 300 6 20 240 Post Heat 25 60 After freeze drying, glucosamine sulfate sodium chloride was obtained as a white powder in a yield of 556 g (97% of theoretical). Example 8 Example 7 was repeated using 1655 g of purified water, 431.5 g (2 moles) of glucosamine hydrochloride and 120.3 g (1 mole) of magnesium sulfate instead of the sodium sulfate. After freeze drying, glucosamine sulfate magnesium chloride was obtained as a white powder in a yield of 530 g (96% of theoretical). Example 9 Example 7 was repeated using 1855 g of purified water, 431.5 g (2 moles) of glucosamine hydrochloride and 287.5 g (1 mole) of zinc sulfate (heptahydrate) instead of the sodium sulfate. After freeze drying, glucosamine sulfate zinc chloride was obtained as a white powder in a yield of 540 g (95% of theoretical). Example 7 was repeated using 1679 g of purified water, 431.5 g (2 moles) of glucosamine hydrochloride and 128 g (1 mole) of lithium sulfate (monohydrate) instead of the sodium sulfate. After freeze drying, glucosamine sulfate lithium chloride was obtained as a white powder in a yield of 525 g (97% of theoretical). Example 11 Example 7 was repeated using 450 g of purified water, 107.8 g (0.5 mole) of glucosamine hydrochloride and 42.3 g (0.25 mole) of manganese sulfate monohydrate instead of the sodium sulfate. After freeze drying, glucosamine sulfate manganese chloride was obtained as a white powder in a yield of 144 g (98% of theoretical). Example 12 The purpose of this example was to measure the specific rotation of mixtures of glucosamine hydrochloride and metal sulfates as distinguished from the glucosamine sulfate metal chloride true compounds of the invention. The mixtures were prepared by mixing glucosamine hydrochloride and the metal sulfate in a 2:1 molar ratio in sufficient purified water to yield a 20 wt.% solution (at 20°C). The solutions were filtered through Whatman #4 filter paper and were then checked (at 20°C) for specific rotation 20 minutes, 2 hours and 24 hours later . The true compounds of the invention obtained by freeze drying as set forth in Examples 3 and 7-11, i.e., the glucosamine sulfate metal chlorides, were dissolved in sufficient purified water to yield 20 wt.% solutions (at 20°C), filtered through Whatman # 4 filter paper and then checked (at 20 °C) for specific rotation 20 minutes, 2 hours and 24 hours later. As may be seen in Table π, the specific rotations of the mixtures consistently change throughout the 24-hour period (at 20°C) whereas the specific rotations of the true compounds of the invention obtained as set forth in Examples 3 and 7-11 remained constant, thus indicating by a simple specific rotation test whether a mixture or a true compound is present. Table π Syn. Mix. = synthetic mixture GHCl = glucosamine hydrochloride; GS = glucosamine sulfate Example 13 The purpose of this example was to measure the tap densities of synthetic mixtures of glucosamine hydro-chloride and metal sulfates and the freeze-dried compounds of the invention. The results are set forth in Table m. Table m Exam le 14 Dibromomethane, 58 cc (144 g), density of 2.48 g cc, was mixed with dichloromethane, 42 cc (56 g), density of 1.3 g/cc, to yield 100 cc of a first solvent having a density of 2.0 g/cc. The first solvent was used to evaluate glucosamine hydrochloride mixed with potassium sulfate, glucosamine hydrochloride mixed with sodium sulfate, glucosamine hydrochloride mixed with magnesium sulfate, glucosamine hydrochloride mixed with zinc sulfate and glucosamine hydrochloride mixed with manganese sulfate as well as the compounds glucosamine sulfate * 2 potassium chloride (Example 3), glucosamine sulfate - 2 sodium chloride (Example 7), glucosamine sulfate * magnesium chloride (Example 8), glucosamine sulfate * zinc chloride (Example 9) and glucosamine sulfate • manganese chloride (Example 11). A second solvent was prepared by mixing dibromomethane, 35 cc (87 g), density of 2.48 g/cc, with 65 g dichloromethane, 65 cc (85 g), density of 1.3 g/cc, to yield 100 cc of a second solvent having a density of 1.7 g/cc. The second solvent was used to evaluate glucosamine hydrochloride mixed with lithium sulfate and the compound glucosamine sulfate * 2 lithium chloride (Example 10). The evaluations of the mixtures and compounds were carried out by placing 2 g of the mixture or compound in a vial together with 10 cc of the first or second solvent and shaking the vial for a few seconds. After allowing the vial to stand for ten minutes, it was noted that the vials containing the mixture showed a layer floating on the surface of the solvent and a precipitate, whereas in the case of the vials containing the compounds, all of the material floated on the surface of the solvent, without the appearance of any precipitate. The mixtures and the compounds were initially assayed by titration for % chloride content prior to mixing with the first or second solvent. After the ten minute period subsequent to the mixing of the mixtures and compounds with the first or second solvent, the surface layers in all of the vials, i.e., the top fractions, as well as the precipitates in all of the vials, i.e., the bottom fractions, were also assayed for % chloride content by titration and their specific rotations were also measured. The results are set forth in Table IV. Table IV en Example 1 In this example, a comparison of the various materials was carried out using the following procedure: A one-liter glass beaker was provided with a paper thimble of 12.1 cm in length and 4.4 cm in diameter. A glass tube with a fritted end having a length of 25.4 cm, an outer diameter of 7.6 mm and an inner diameter of 5.1 mm was inserted into the thimble such that the end thereof was approximately 5 mm from the bottom of the thimble. Glucosamine salts and glucosamine compounds prepared as synthetic mixtures and by the freeze-drying method of the invention, respectively, in the amount of 50 g for each salt and each compound were placed in the thimble and the open end of the glass tube was connected to a nitrogen gas cylinder. Nitrogen was sparged through the frit at the rate of 56.6 liters/minute for approximately 15 minutes and lighter material cascaded over the thimble and was collected in the beaker. The material in the thimble was assayed by titration for chloride prior to commencement of nitrogen sparging (initial assay). The fraction sparged out was measured for specific rotation and also assayed by titration for % chloride. The fraction remaining in the thimble was measured for specific rotation. The results are set forth in Table V. Table V As may be seen from Table V, the synthetic mixtures and the compounds of the invention, had satisfactory initial assays, before nitrogen sparging. However, after sparging, the assays obtained for the synthetic mixtures from the material sparged out of the thimble were considerably different from the initial assays indicating that such materials were mixtures and not true compounds. This was further reinforced by the different specific rotation values obtained in respect to the material sparged out versus those of the material remaining in the thimble. On the other hand, the materials prepared by the freeze drying method recited in Examples 1-5 above were clearly true compounds as evidenced by no change in the assay values prior to, and subsequent to, sparging as well as the top fraction and the remaining fraction having the same specific rotation values, after sparging.

Claims: WHAT IS CLAIMED IS: 1. A composition comprising: (a) the compound glucosamine sulfate metal chloride, wherein the metal is selected from the group consisting of potassium, sodium, magnesium, zinc, lithium and manganese, said compound having a purity level of at least about 97%; and (b) water, present in a maximum amount of about 10 wt.%, based on the weight of the composition. 2. The composition of claim 1 wherein the purity level is at least 99%. 3. The composition of claim 1 wherein water is present in a maximum amount of 5 wt.%, based on the weight of the composition. 4. The composition of claim 3 wherein the water is present in a maximum amount of 3 wt.%, based on the weight of the composition. 5. The composition of claim 1 wherein the metal comprises potassium. 6. The composition of claim 1 wherein the metal comprises sodium. 7. The composition of claim 1 wherein the metal comprises magnesium. 8. The composition of claim 1 wherein the metal comprises manganese. 9. A process for preparing a composition comprising the compoimd glucosamine sulfate metal chloride, wherein the metal is selected from the group consisting of potassium, sodium, magnesium, lithium, zinc and manganese, said compoimd having a purity level of at least about 97%, which comprises the steps of: (a) contacting glucosamine hydrochloride with a sulfate of said metal in the presence of water to form an aqueous solution of glucosamine sulfate metal chloride; and (b) recovering the compound by freeze-drying the solution from step (a) at a temperature and at a reduced pressure for such period of time that: (i) at least about 90 wt.% of the water is removed and (ii) decomposition of the compound glucosamine sulfate metal chloride is limited to a maximum of about 3%. 10. The process of claim 9 wherein the glucosamine hydrochloride and metal sulfate are contacted in stoichiometric quantities in the presence of sufficient water to form a concentration of solids of about 15 to 45 wt.%, and the contacting in step (a) takes place for a period of about 15 minutes to 2 hours. 11. The process of claim 9 wherein the water is present in step (a) in an amount such that the concentration of solids is in the range of 20 to 35 wt.%, based on the weight of water plus solids. 12. The process of claim 9 wherein step (a) takes place at a temperature in the range ofabout 20 to 45°C. 13. The process of claim 9 wherein the freeze-drying is carried out at a pressure of not greater than about 800 milliTorr and at a temperature in the range of about -60°C to O°C. 14. The process of claim 13 wherein the freeze-drying is carried out at a pressure in the range of 300 to 500 milliTorr and a temperature in the range of -40 to -5°C. 15. The process of claim 9 wherein the metal sulfate comprises potassium sulfate. 16. The process of claim 9 wherein the metal sulfate comprises sodium sulfate. 17. The process of claim 9 wherein the metal sulfate comprises magnesium sulfate. 18. The process of claim 9 wherein the metal sulfate comprises manganese sulfate.

Inventors: BURGER CHRISTOPHER M, CHOPDEKAR VILAS M, SCHLECK JAMES R, BURGER, CHRISTOPHER, M., CHOPDEKAR, VILAS, M., SCHLECK, JAMES, R.
Applicants: JAME FINE CHEMICALS INC, JAME FINE CHEMICALS, INC.
Application year: 1999
Main classification: C07H5
IPC codes: C07H5, C07H11