High purity crystalline forms of peptides Arg-Lys-Asp and Arg-Lys-Asp-Val, process for preparing them and pharmaceutical compositions containing them

Abstract: The present invention relates to a process for the preparation of high purity crystalline forms of peptides Arg-Lys-Asp and Arg-Lys-Asp-Val from crude, amorphous peptides Arg-Lys-Asp and Arg-Lys-Asp-Val. The process is characterized in that the crude, amorphous peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val is allowed to stand at room temperature with 5 to 20 unit volume of an ethanolic solution containing 0.5 to 4.0% by volume of acetic acid and 5 to 25% by volume of water, wherein the volume unit is calculated for the mass unit of the material and mass unit relates to volume unit as g relates to ml, then the crystallized peptide is separated from the crystalline suspension, preferably after cooling. Pharmaceutical compositions containing the crystalline forms of these peptides are also described.

Description: The invention relates to crystalline forms of peptide Arg-Lys-Asp and Arg-Lys-Asp-Val of high purity, to pharmaceutical compositions containing them and to a process for the preparation of these peptides and pharmaceutical compositions containing them. The Hungarian patent specification No. 185,263 discloses the peptides Arg-Lys-Asp and Arg-Lys-Asp-Val and their action influencing the immune system. Several publications describe their wide-range in vitro and in vivo immunological and immunopharmacological effects: see e.g. Hoope Seyler's Z. Physiol. Chem., 364 , 933. (1983); J. Immunopharmacol., 7 , 67 (1985) ; Int. J. Immunopharmacol., 8 , 167 (1986); Immunpharmacol. Immunotoxicol., 9 , 1 (1987). In the knowledge of the advantageous biological results the detailed toxicological and clinical examination of these two peptides has been carried out. For the preparation of a clinically usable drug the synthesis of the peptides has to be carried out on an industrial scale in the magnitude of several kilogramms per batch so that high purity products can be prepared which correspond to the strict regulations necessary for pharmaceutical compositions. During the synthesis described in the Hungarian patent specification No. 185,263 of the two peptides, the amino and carboxyl groups are protected by benzyl type protecting groups and the guanidino group of arginine is protected by a nitro group. In the last step all the protecting groups are removed by catalytic hydrogenation. The conditions under which this combination of the protecting groups works encumber the extension of the reaction and/or its realization on an industrial scale. Further, the quality of the product obtained by hydrogenation is far below the current pharmacological requirements. Accordingly, another synthesis route was elaborated. In the Hungarian patent application No. 3037/88 published under No. T/50195 only a tert-butyl-type protecting group is used during the synthesis of the structural and optical isomers of the peptides of the present invention and the guanidino group of arginine is protected by protonation. The protecting groups are removed in one step by using trifluoroacetic acid in a known manner. The synthesis route described in Hungarian patent application No. 3037/88 eliminates a great part of the side reactions of the synthesis described in the Hungarian patent specification No. 183,263 and the product obtained is more pure. However, the extension and the industrial scale realization of this process is expensive, invoLves several technical and environmental problems and spoils the quality. In human therapy a peptide purity of more than 97% is generally acceptable and the quantity of any single contamination may surpass 0.5% only if its structure is known and its innocuity has been proved by toxicological tests. According to the processes described in the Hungarian patent specification No. 185,263 and Hungarian patent application No. 3037/88 the tripeptide Arg-Lys-Asp and the tetrapeptide Arg-Lys-Asp-Val were separated and purified either after ion exchange by lyophilization or after evaporation by ethanolic treatment. In both processes the tripeptide Arg-Lys-Asp and the tetrapeptide Arg-Lys-Asp-Val were isolated in amorphous state. Both amorphous and air dried substances contain 70 to 85% of a peptide, the rest consists of water, acetic acid and ethanol. Lyophilized substances generally contain 15% of acetic acid. Both the water and the acetic acid content significantly depend on the reaction conditions used (e.g. starting substance concentration, lyophilization program, drying time and temperature). The solvent content of the substance isolated by ethanol after the ion exchange is actively reflected in the changes in the technological parameters used and the ethanol could not be removed from some amorphous samples even after modifying the drying parameters within wide ranges. Their amorphous structure has been shown by x-ray diffraction pictures made with a powdery form. No sharp peaks showing crystalline structure can be observed. The thermogravimetric measurements and differential calorimetric tests unambiguously prove that the peptides in question bind a part of the accompanying solvent to them by adsorption and thus the quantity and ratio of peptides to solvents varies very widely, presumably due to smaller undetermined changes in the technological parameters and e.g. by the changing moisture content of the surroundings. The last effect could have unambiguously been proved by a thermogravimetric test. The slightly dissected wide strip between 1700 and 1400 cm⁻¹ in the infrared spectrum shows the presence of water bound only by adsorption. Because of the amorphous state of the peptides even the quantity of the accompanying acetic acid is not stoichiometric and the quantity of the water and ethanol also fluctuates within wide ranges. In some countries the official stipulations for pharmaceutical starting substances allow neither a fluctuation of the quantity of the accompanying solvents within wide ranges nor the quantity of ethanol to reach 6 to 7%. The fluctuating peptide content of the products thus makes the adjustment of the desired dose very uncertain during the preparation of the pharmaceutical compositions. No crystalline substances of stoichiometric composition could be prepared by the known processes either through reprecipitation or treatment with a solvent of the oil obtained after ion exchange or of the solid, amorphous substance obtained from said oil. Surprisingly, we have now found that the peptides Arg-Lys-Asp and Arg-Lys-Asp-Val obtained by the processes described in the Hungarian patent specification No. 185,263 and Hungarian patent application No. 3037/88 can be made crystalline by a post-reaction treatment with a water-ethanol mixture, containing also a small amount of acetic acid. Thus, according to one aspect of the present invention, there is provided a process for the preparation of a high purity crystalline form of the peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val from crude, amorphous Arg-Lys-Asp or Arg-Lys-Val respectively, characterised in that crude, amorphous peptide Arg-Lys-Asp or Arg-Lys-Asp-Val, is allowed to stand at room temperature in 5 to 20 unit volume of an ethanolic solution containing 0.5 to 4.0% of volume of acetic acid and 5 to 25% by volume of water, wherein the volume unit is calculated for the mass unit of the peptide and mass unit relates volume unit as g relates to ml, then the crystallized peptide is separated from the crystalline suspension. The separation is preferably carried out after cooling of the suspension. One may preferably proceed by using 10 units of volume of the above solvent mixture calculated for one mass unit of the crude peptide. The water content of the solvent mixture is adjusted in the case of peptide Arg-Lys-Asp preferably to 10% by volume and in the case of peptide Arg-Lys-Asp-Val preferably to 19% by volume. These prefered compositions of the solvent system promote the forming of crystals of a composition nearing "acetate-dihidrate" in the first case and "acetate-monohydrate" in the second case. The process of the invention is preferably carried out by keeping the crude peptide in the previously prepared solvent mixture for several days until it becomes crystalline. The amorphous substance first slightly softens and becomes oily and then slowly crystallizes. The crystallization may be enhanced by cooling. The crystalline peptide is separated preferably by filtration from the mother liquor. After filtration the crystalline substance is washed with aqueous ethanol and dried under air or in an exsiccator. When crystallizing the peptide Arg-Lys-Asp-Val one may also proceed by dissolving the crude peptide in water containing the appropriate amount of acetic acid, then the calculated amount of ethanol is thereafter. The separation and processing of the precipitated crystalline product may be carried out as described above. The process of the invention may successfully be applied in the case of both lyophilized crude peptides and crude peptides isolated by ethanol or by aqueous ethanol. The process is reproducible and may be enlarged to industrial scales. The present invention is surprising since other, similar peptides, e.g. L-arginyl-L-lyzyl-D-asparginic acid, i.e. the diastereomer compound also disclosed in Hungarian patent application No. 3037/88, cannot be made crystalline in this way. The x-ray diffraction sprectrum of the crystalline peptides obtained from the process of the present invention is strongly dissected as related to the amorphous peptide used as starting substance. A great number of peaks relating to the crystalline structure appears therein. In the IR spectrum a sharp peak appears between wave numbers 3300 and 3400 cm⁻¹ indicating the presence of crystal water. The thermogravimetric curve taken with crystalline substances shows, in relation to amorphous substances, much stronger changes taking place within narrower temperature ranges. The crystalline forms of the peptides prepared according to the process of the present invention possess very high purity. The purity of Arg-Lys-Asp basedcrystalssurpasses 99%, the substance contains 0.7 to 0.8 mole/mole acetic acid, nearly 2 mole/mole water and less than 0.5% by weight of ethanol. The melting point of the different samples varies between 147 and 158°C (during decomposition) in a wide range of 4°C maximum. The crystalline form of peptide Arg-Lys-Asp-Val contains about 0.8 mole/mole acetic acid, about 1 mole/mole water and less than 1% by weight of ethanol. The melting point of the different samples varies between 208 and 218 °C (during decomposition) in a wide range of 4°C maximum. The crystalline state of the peptides prepared by the process of the invention is proved, in addition to their determined melting points, by their thermogravimetric and differential calorimetric examinations and x-ray diffraction pictures.These crystalline substances having a well defined composition are much more pure according to detailed quality control tests than the amorphous products. Due to their crystalline state they are more stable, their storage is safer, and they are not as sensitive to the environmental effects (e.g. temperature and humidity) as the amorphous peptides. The enteral administration of the known amorphous peptides requires complicated and expensive encapsulating methods as the variable pharmaceutical compositions and the changeability caused by environmental effects excludes the possibility of the preparation of tablets. On the contrary, the forms of the peptides prepared by the process of the present invention are suitable for the preparation of solid forms of drugs, thereby facilitating their oral administration. Thus, a further feature of the present invention is a pharmaceutical composition comprising a high purity crystalline form of peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val in admixture with one or more pharmaceutically acceptable diluents, excipients or diluents. A yet further feature of the present invention is a process for the preparation of a pharmaceutical composition as described above which comprises the admixing of a high purity crystalline form of peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val with one or more pharmaceutically acceptable diluents, excipients or carriers. Further details of the process according to the present invention are illustrated by the following non-limiting examples. The abbreviations used in the specification correspond to the abbreviations generally used in the art [Biochem J., 219 , 345 (1984)]. In the symbolic names of the compounds the amino acid groups are of L-configuration corresponding to the general labelling practice. The thin layer chromatography tests were carried out on prefabricated silica gel adsorbent (DC-Fertigplatten, Merck, FRG) with the following solvents (the ratios are always by volume; the stock solution is a 20:6:11 mixture of pyridine, acetic acid and water): 1. 3:7 mixture of n-butanol and stock solution 2. 2:8 mixture of n-butanol and stock solution 3. 1:1:1:1 mixture of n-butanol, acetic acid, ethyl acetate and water The chromatograms were developed by ninhydrine and after chlorination by a potassium iodide/tolydine reagent. The high pressure liquid chromatography measurements were performed on equipment furnished with a Labor-MIM (a Hungarian company) type loop injector, a feeding pump and pressure indicator consisting of Gilson 802C and 302 units and an HP 3300A type integrator. For the separation a charge of the following parameters was used: grain size = 6 µm, phase = C18, length = 250 mm and internal diameter = 4.6 mm (produced by Bioszeparációs Gmk, Hungary). As eluent a 10% aqueous phosphorous acid solution was used. The peptide Arg-Lys-Asp was tested with this solution while 3% by volume of acetonitrile was added to this eluent for the testing of the peptide Arg-Lys-Asp-Val. The measuring was carried out at a stream ratio of 1 ml/minute and the light absorption of the solution was detected at 212 nm. The specific rotatory power was determined by a Perkin-Elmer 241 type polarimeter. All the evaporations were carried out on a Büchi type rotary vacuum evaporator on a water bath of 40°C. The melting points were determined by a Tottoli type (Büchi) measuring device. The thermogravimetric and differential calorimetric measurements were carried out with a Mettler type TA 3000s DSC 20 T650 combined device. The x-ray diffraction pictures were taken by a Philips W 1840 type diffractometer. The amino acid analysis of the end products was carried out in a Biotronic LC 5001 type device. The samples were hydrolized in a 6 moles/l hydrochloric acid solution at a temperature of 110 °C for 24 hours. The results were within the ± 5% limit of error in all cases. Example 1 Crystallization of Arg-Lys-Asp 31 g of amorphous tripeptide Arg-Lys-Asp containing 85% of the peptide are sprinkled into 310 ml of a mixture containing 86 parts by volume of ethanol, 13 parts of water and 1 part of acetic acid and the adhered substance is broken up from time to time with a spatula until it fully transforms into granular crystals. The beginning of the crystal formation is visible to the naked eye after about 15 hours. After 3 days the mixture is put into a refrigerator for several hours and then the suspension is filtered, washed twice with 45 ml of the above described solvent mixture each and dried under air until its mass becomes constant. Thus 29.0 g of an end product is obtained which melts at 154 to 157 °C while decomposing. Its purity surpasses 99% as proved by both thin layer chromatography and high pressure liquid chromatography. R 1 f =0.08; R 2 f =0.15; R 3 f =0.20. Amino acid analysis: Asp=1.00 (1), Lys=0.97 (1), Arg=1.01 (1). [α] 25 D =+3.4° (c=1; 10% acetic acid); [α] 25 D =+9.1° (c=1; acetic acid). The peptide content of the different samples obtained by the repeated performance of the procedure described in Example 1 amounted to 80 to 83%, their ethanol content was less than 0.5%, their water content varied between 6.5 and 8.0% and acetic acid content between 8 and 10%. Example 2 Crystallization of Arg-Lys-Asp-Val 13.8 g amorphous tetrapeptide Arg-Lys-Asp-Val containing 83% of the peptide are treated with a mixture of 26 ml of water, 1.5 ml of acetic acid and 110 ml of ethanol as described in Example 1. The beginning of the crystal formation is visible to the naked eye after about 10 hours. After 2 days the mixture is put into a refrigerator for several hours, then the suspension is filtered, washed twice with 30 ml of 80% by volume of ethanol each and dried under air until the mass becomes constant. Thus 13.0 g of an end product is obtained which melts at 212 to 215 °C while decomposing. Its purity surpasses 99% as proved by both thin layer chromatography and high pressure liquid chromatography. R 1 f =0,15; R 3 f =0.30. Amino acid analysis: Asp=1.00 (1), Lys=1.02 (1), Arg=1.01 (1), Val=0.97 (1). [α] 25 D =-22.4 ° (c=1; 0.1 mole/l acetic acid). The peptide content of the different samples obtained by the repeated performance of the procedure described in Example 2 amounted to 84 to 88%, their ethanol content was less than 1%, their water content varied between 3 and 5% and acetic acid content between 8 and 10%. Example 3 Crystallization of Arg-Lys-Asp-Val 13.8 g of amorphous tetrapeptide Arg-Lys-Asp-Val containing 83% of the peptide are dissolved in a mixture of 26 ml of water and 1.5 ml of acetic acid while shaking, then the solvent is diluted with 110 ml of ethanol. The crystalline title product slowly precipitates from the pure solution. The beginning of the nodule formation can be observed after 10 hours. After 2 days the mixture put in a refrigerator for several hours, then it is filtered and the precipitate is washed twice with 30 ml of 80% by volume of aqueous ethanol each and dried in air. Thus 12.8 g of a crystalline tetrapeptide is obtained which melts at 212 to 215 °C while decomposing. Its purity surpasses 99% as proved by both thin layer chromatography and high pressure liquid chromatography. R 1 f =0,15; R 3 f =0.30. Amino acid analysis: Asp=1.01 (1), Val=0.98 (1), Lys=1.02 (1). Arg=1.01 (1). [α] 25 D =-22.4° (c=1; 0.1 mole/l acetic acid).

Claims: Claims for the following Contracting States : AT, BE, CH, LI, DE, DK, FR, GB, IT, LU, NL, SE Process for the preparation of a high purity crystalline form of the peptide Arg-Lys-Asp or the peptide Arg-Lys-Asp-Val from crude, amorphous peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val respectively, characterized in that the crude, amorphous peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val respectively is allowed to stand at room temperature with 5 to 20 unit volume of an ethanolic solution containing 0.5 to 4.0% by volume of acetic acid and 5 to 25% by volume of water, wherein the volume unit is calculated for the mass unit of the material and mass unit relates to volume unit as g relates to ml, then the crystallized peptide is separated from the crystalline suspension. A process as claimed in Claim 1 wherein the peptide/solvent mixture is cooled prior to crystal separation. A process as claimed in Claim 1 or Claim 2 wherein 10 units by volume of solvent mixture calculated for 1 mass unit of crude amorphous peptide is used. A process as claimed in any one of Claims 1 to 3 wherein a solvent mixture containing 1% by volume of acetic acid is used. A process as claimed in any of Claims 1 to 4 for the preparation of a high purity crystalline form of peptide Arg-Lys-Asp wherein a solvent mixture containing 10% by volume of water is used. A process as claimed in any of Claims 1 to 4 for the preparation of a high purity crystalline form of peptide Arg-Lys-Asp-Val wherein a solvent mixture containing 19% by volume of water is used. A process as claimed in any of Claims 1 to 4 and 6 for the preparation of a high purity crystalline form of peptide Arg-Lys-Asp-Val wherein the amorphous peptide Arg-Lys-Asp-Val is first dissolved in a mixture of the water and acetic acid and the calculated amount of ethanol is added thereafter. A crystalline form of peptide Arg-Lys-Asp obtainable by a process according to any one of Claims 1 to 5. A crystalline form of peptide Arg-Lys-Asp-Val obtainable by a process according to any one of Claims 1 to 4, 6 and 7. A pharmaceutical composition comprising a high purity crystalline form of peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val in admixture with one or more pharmaceutically acceptable diluents, excipients, or carriers. A process for the preparation of a pharmaceutical composition as defined in Claim 10 which comprises the admixing of a high purity crystalline form of peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val with one or more pharmaceutically acceptable diluents, excipients or carriers. A crystalline form of Arg-Lys-Asp. A crystalline form of Arg-Lys-Asp-Val. Claims for the following Contracting States : ES, GR Process for the preparation of a high purity crystalline form of the peptide Arg-Lys-Asp or the peptide Arg-Lys-Asp-Val from crude, amorphous peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val respectively, characterized in that the crude, amorphous peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val respectively is allowed to stand at room temperature with 5 to 20 unit volume of an ethanolic solution containing 0.5 to 4.0% by volume of acetic acid and 5 to 25% by volume of water, wherein Llie volume unit is calculated for the mass unit of the material and mass unit relates to volume unit as g relates to ml, then the crystallized peptide is separated from the crystalline suspension. A process as claimed in Claim 1 wherein the peptide/solvent mixture is cooled prior to crystal separation. A process as claimed in Claim 1 or Claim 2 wherein 10 units by volume of solvent mixture calculated for 1 mass unit of crude amorphous peptide is used. A process as claimed in any one of Claims 1 to 3 wherein a solvent mixture containing 1% by volume of acetic acid is used. A process as claimed in any of Claims 1 to 4 for the preparation of a high purity crystalline form of peptide Arg-Lys-Asp wherein a solvent mixture containing 10% by volume of water is used. A process as claimed in any of Claims 1 to 4 for the preparation of a high purity crystalline form of peptide Arg-Lys-Asp-Val wherein a solvent mixture containing 19% by volume of water is used. A process as claimed in any of Claims 1 to 4 and 6 for the preparation of a high purity crystalline form of peptide Arg-Lys-Asp-Val wherein the amorphous peptide Arg-Lys-Asp-Val is first dissolved in a mixture of the water and acetic acid and the calculated amount of ethanol is added thereafter. A process for the preparation of a pharmaceutical composition which comprises the admixing of a high purity crystalline form of peptide Arg-Lys-Asp or peptide Arg-Lys-Asp-Val with one or more pharmaceutically acceptable diluents, excipients or carriers.

Inventors: DENES LASZLO DR, GAZDAG MARIA DR, HAJOS GYOE-RGY DR, IVANYI GEZA, KOVACS LAJOS, LORANT GIZELLA, MUCK ZSUZSANNA, NYEKI OLGA, PETER IMRE, SCHON ISTVAN DR, SZPORNY LASZLO DR, UBERHARDT ILDIKO, UBERHARDT TAMAS, DENES, LASZLO,DR., GAZDAG, MARIA DR., HAJOS, GYOE-RGY, DR., IVANYI, GEZA, KOVACS, LAJOS, LORANT, GIZELLA NEE MAREK, MUCK, ZSUZSANNA NEE KEREPESI, NYEKI, OLGA, PETER, IMRE, SCHON, ISTVAN DR., SZPORNY, LASZLO, DR., UBERHARDT, ILDIKO NEE FALUDI, UBERHARDT, TAMAS, Hajos, Gyö-rgy, Dr., Ivanyi, Géza, Lorant, Gizella née Marek, Muck, Zsuzsanna née Kerepesi, Uberhardt, Ildiko née Faludi, Uberhardt, Tamàs
Applicants: RICHTER GEDEON VEGYESZET, RICHTER GEDEON VEGYESZETI GYAR R.T.
Application year: 1991
Main classification: C07K1
IPC codes: A61K38, C07K1, C07K5, A61P37