Patent Application
20050032818
The present invention relates to the anxiolytic, antiepileptic, sedative hynotic and skeletal muscle relaxing agent zaleplon. More particularly, the invention relates to late stage processing of zaleplon and to particular crystal forms of the drug accessible by adjustments in the late stage processing. The invention further relates to N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-5-yl)phenyl]-N-ethylacetamide (4), regioisomer of zaleplon. Then invention further relates to HPLC methods for the analysis and assay of zaleplon.
Zaleplon possesses anxiolytic, antiepileptic, sedative and hyponotic properties. It is approved by the U.S. Food and Drug Administration for short-term treatment of insomnia and is available by prescription under the brand name Sonatas®. The molecular structure of zaleplon is known and may be represented as:
The IUPAC name of zaleplon is N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-7-yl)phenyl]-N-ethylacetamide.
U.S. Pat. No. 4,626,538 (“the '538 patent”) provides a general methodology for preparing zaleplon and structurally related compounds. In Example 2 of the '538 patent, N-(3-acetylphenyl)ethanamide 1 is reacted with dimethylformamide dimethyl acetal to form N-[3-[3-(dimethylamino)-1-oxo-2-propenyl)]phenyl]-N-acetamide 2. In Example 7 of the '538 patent, the primary amide of acetamide 2 is alkylated with ethyl iodide, forming N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide 3. Zaleplon was prepared in Example 14 by condensing ethylacetamide 3 and 3-amino-4-cyanopyrazole 4 in refluxing glacial acetic acid. Zaleplon was worked up by partitioning the non-volatiles between saturated sodium bicarbonate and dichloromethane, drying the organic phase, passing the organic phase through an adsorbent (magnesium silicate), adding hexane to the organic phase, cooling the organic phase and collecting a solid that forms in the organic phase. The product is reported to have a melting point of 186-187° C. The overall synthesis is depicted in Scheme 1. The '538 patent does not indicate that byproducts were formed in any of the reactions or explain how byproducts could be separated from zaleplon if they did form.
U.S. Pat. No. 5,714,607 (“the '607 patent”) describes an improved process for preparing zaleplon. According to the '607 patent, zaleplon can be obtained in improved yield and purity if the final step of the '538 patent process is modified by adding water to the acetic acid solvent at about 10% to about 85% (v/v). As stated in the '607 patent, the improved conditions shorten the reaction time from about 3-3.5 h to about 1-3.5 hours. According to Table 1 of the '607 patent, zaleplon was obtained in yields ranging from 81.7-90% and in HPLC purity ranging from 98.77 to 99.4%. In each of the examples, zaleplon was obtained by crystallization out of the reaction mixtures, which were mixtures of water and acetic acid. The '538 patent does not indicate that byproducts were formed in the process or explain how byproducts could be separated from zaleplon if they were to form.
In order to obtain marketing approval for a new drug product, manufacturers have to submit to the regulatory authorities evidence to show that the product is acceptable for human administration. Such a submission must include, among other things, analytical data to show the impurity profile of the product to demonstrate that the impurities are absent, or are present only a negligible amount. For such a demonstration there is a need for analytical methods capable of detection of the impurities and reference standards for identification and assaying thereof. There is also a need for reference standards in such analytical methods.
The U.S. Food and Drug Administration's Center for Drug Evaluation and Research (CDER) has promulgated guidelines recommending that new drug and generic drug applicants identify organic impurities of 0.1% or greater in the active ingredient. “Guideline on Impurities in New Drug Substances” 61 Fed. Reg. 371 (1996), “Guidance for Industry ANDAs: Impurities in Drug Substances” 64 Fed. Reg. 67917 (1999). Unless an impurity is a human metaboiite, has been tested for safety, or was present in a composition that was shown to be safe in clinical trials, the CDER further recommends that the drug applicant reduce the amount of the impurity in the active ingredient to below 0.1%. Thus, there is a need to isolate impurities in drug substances so that their pharmacology and toxicology can be studied.
Crystalline forms, that include polymorphs and pseudopolymorphs, are distinct solids sharing the same structural formula, yet having different physical properties due to different conformations and/or orientations of the molecule in the unit cell. One physical property that can vary between crystalline forms is solubility, which can affect the drug's bioavailability. Crystalline forms of a compound can be differentiated in a laboratory by powder X-ray diffraction spectroscopy. For a general review of crystalline forms (i.e. polymorphs and pseudopolymorphs) and the pharmaceutical applications of polymorphs see G.M. Wall, Pharm. Manuf. 3, 33 (1986); J. K. Haleblian and W. McCrone, J. Pharm. Sci., 58, 911 (1969); and J. K. Haleblian, J. Pharmn. Sci., 64, 1269 (1975).
The discovery of new crystalline forms of a pharmaceutically useful compound provides a new opportunity to improve the performance characteristics of a pharmaceutical product. It enlarges the repertoire of materials that a formulation scientist has available for designing, for example, a pharmaceutical dosage form of a drug with a targeted release profile or other desired characteristic. The present invention provides four new crystalline forms of zaleplon.
N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-5-yl)phenyl]-N-ethylacetamide 5 having the structural formula
forms as a minor byproduct in the condensation step of the reaction disclosed in U.S. Patent Application Publication No. 2003/0040522. This compound is previously unknown in the chemical literature and, as discussed below, it can serve as a reference standard in the analysis of zaleplon. Compound 5 is a regioisomer of zaleplon that differs from zaleplon in the position of the N-ethyl-N-acetylaminophenyl group on the fused heterocyclic ring system. The formation of regioisomer 5 can be accounted for by either (1) a 1,2 addition of the 3-amino group of cyanopyrazole 4 with elimination of water and Michael-type addition of the 2-nitrogen atom of the pyrazole onto the conjugated C═C double bond or (2) a Michael addition of the 2-nitrogen atom of the pyrazole and cyclization of the 3-amino group onto the keto group. By whatever mechanism regioisomer 5 forms, the salient fact is that it is an undesired minor byproduct in viable commercial preparations of zaleplon.
Under the conditions set forth in U.S. Patent Application Publication No. 2003/0040522, regioisomer 5 typically forms to the extent of about 0.2 to 0.5% relative to the desired isomer.
Thus, in one aspect, the present invention relates to N-[3-(3-cyanopyrazolo[1,5a]pyrimidin-5-yl)phenyl]-N-ethylacetamide, which is referred to as zaleplon regioisomer or regioisomer of zaleplon. This new compound, which is characterized by NMR and MS investigations, can be used as a reference marker in analysis of zaleplon.
In still a further aspect, the present invention relates to analytical methods for testing and show the impurity profile of zaleplon. These methods are also suitable for analyzing and assaying zaleplon and its main impurity which, in the methods of the invention, serves as reference marker.
In another aspect, the present invention relates to a method of making N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-5-yl)phenyl]-N-ethylacetamide including the steps of reacting a mixture of N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide, 3-amino-4-cyanopyrazole, and a strong acid in a liquid reaction medium of water and at least one water-miscible organic compound free of carboxylic acid groups, neutralizing the reaction mixture to precipitate crude product, and separating N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-5-yl)phenyl]-N-ethylacetamide from other components of crude product by chromatography on a silica gel column using a mixture of chloroform and acetone as eluent, wherein the amount of strong acid, on a mole basis, is at least 10 times the amount of either N-[3-[3-(dirmethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide or 3-amino-4-cyanopyrazole, whichever is in excess, or of either of them if they are used in approximately equimolar amounts.
Zaleplon and regioisomer 5 are difficult to separate because of their structural similarity. There is a need in the pharmaceutical arts for a process of purifying zaleplon that is in mixture with the regioisomer. The present invention meets this need with a precipitation process that is effective at separating the two compounds. It will be understood that the present method of purifying zaleplon is effective in reducing or eliminating many other impurities as well.
In another aspect, the present invention provides a process for purifying zaleplon that can be in mixture with zaleplon regioisomer and other impurities by precipitating a solid enriched in zaleplon from a solution formed from a crude zaleplon from any source. The solution can be formed by dissolving crude zaleplon in an organic solvent at elevated temperature, wherein the organic solvent is selected from the group consisting of alcohols, ketones, ethers, carboxylic acids, carboxylic acid esters, nitrites, aromatic hydrocarbons, and halogenated hydrocarbons, mixtures of any of them, and mixtures of one or more of them with water. Purified zaleplon can be precipitated from the solution by cooling the solution from the elevated temperature, by use of an anti solvent, or by use of an antisolvent and cooling. In one embodiment of the process, an antisolvent is added to the solution at elevated temperature. By means of the purification process, zaleplon essentially free of regioisomer and other impurities can be obtained.
Characterization of the essentially pure zaleplon obtained from the purification process led to the discovery that certain process embodiments produce novel crystalline forms of zaleplon, wherefor the present invention further provides novel crystalline forms of zaleplon that are accessible by the stepwise procedure of the purification process by appropriate selection of solvent, antisolvent and/or other conditions.
Thus, in one aspect, the present invention provides crystalline zaleplon Form II characterized by a powder X-ray diffraction pattern having peaks at 7.9, 10.7, 12.5, 14.9, 16.9, 17.9, 21.3, 24.0, 25.2, 25.9, 27.0 and 27.5±0.2 degrees two-theta.
In another aspect, the present invention provides crystalline zaleplon Form III characterized by a powder X-ray diffraction pattern having peaks at 15.4, 18.1, 21.1, 26.8, and 27.5±0.2 degrees two-theta.
In yet another aspect, the present invention provides crystalline zaleplon Form III characterized by a powder X-ray diffraction pattern having peaks at 15.4, 18.1, 21.1, 26.8, and 27.5±0.2 degrees two-theta and further characterized by x-ray diffraction peaks (reflections) at 11.6, 17.6, 19.0, 20.0, and 22.2 degrees two-theta.
In still a further aspect, the present invention provides rystalline zaleplon Form IV characterized by a powder X-ray diffraction pattern having peaks at 8.1, 14.5, 17.3, 21.3±0.2 degrees two-theta.
In another aspect, the present invention provides crystalline zaleplon Form IV characterized by a powder X-ray diffraction pattern having peaks at 8.1, 14.5, 17.3, 21.3±0.2 degrees two-theta and further characterized by by x-ray diffraction peaks at 10.6, 11.1, 14.1, 15.6, 18.0, 18.2, 20.1, 20.3, 24.3, 25.0, 25.9, 26.7, 27.9 and 29.5±0.2 degrees two-theta.
In still another aspect, the present invention relates to crystalline zaleplon in form V characterized by x-ray diffraction peaks at 8.0, 14.8, and 17.0±0.2 degrees two-theta.
In still yet another aspect, the present invention relates to zaleplon in form V characterized by x-ray diffraction peaks at 8.0, 14.8, and 17.0±0.2 degrees two-theta and furthercharacterized by x-ray diffraction peaks at 10.7, 11.0, 12.5, 15.4, 16.5, 17.7,21.3,25.7, and 26.5±0.2 degrees two-theta.
In another aspect, the present invention provides a process for making zaleplon in crystal Form II including the steps of: forming a solution of zaleplon in an organic solvent that is miscible or appreciably soluble in water; contacting the solution with water to induce crystallization of zaleplon, and separating zaleplon Form II from the organic solvent and water.
In another aspect, the present invention provides a process for making zaleplon in crystalline Form II including the steps of: forming a solution of zaleplon in an organic solvent that is miscible with or appreciably soluble in water, contacting the solution with three times its volume of water, optionally cooled to about 0° C., to induce crystallization of zaleplon, and separating zaleplon Form II from the organic solvent and water.
In another aspect, the present invention provides a process for making crystalline zaleplon in Form III including the steps of: forming a solution of zaleplon in acetonitrile, adding water to the solution at elevated temperature, precipitating zaleplon from the solution by cooling, and separating zaleplon Form III from the acetonitrile and water.
In still a further aspect, the present invention provides a process for preparing crystalline zaleplon in Form IV including the steps of: forming a solution of zaleplon in a solvent system selected from the group consisting of 2-propanol and mixtures of tetrahydrofuran and water, precipitating zaleplon from the solution, and separating zaleplon Form IV from the solvent system.
The present invention further provides novel processes for making a known crystalline form of zaleplon.
Thus, in one aspect, the present invention provides a process for preparing zaleplon in Form I including the steps of: forming a suspension of zaleplon in a liquid at elevated temperature, which liquid can be boiling water or a high boiling hydrocarbon, to mention just two, cooling the suspension, and separating zaleplon Form I from the liquid.
In another aspect, the present invention provides a process for making zaleplon in Form I including the steps of: melting zaleplon, solidifying the zaleplon by cooling, and grinding the solidified zaleplon to yield zaleplon Form I.
In still a further aspect, the present invention provides a process for making crystalline zaleplon in form I including the steps of: Dissolving zaleplon in an organic solvent by heating, optionally adding an apolar organic antyisolvent to the resulting solution, inducing precipitation of zaleplon by cooling, and separation of zaleplon Form I.
In yet still a further aspect, the present invention relates to a process for preparing zaleplon in Form I including the steps of: dissolving zaleplon in an organic solvent by heating, addition of an apolar organic antisolvent to the solution, inducing precipitation of zaleplon by cooling, and separation of zaleplon Form I.
Pharmaceutical compositions containing any of the crystal forms of zaleplon herein described—alone or in any combination—are also provided, as are methods of treating, for example, insomnia using any of these pharmaceutical compositions.
In still another aspect, the present invention provides HPLC methods for the analysis and assay of zaleplon.
In another aspect, the present invention provides a HPLC method of assaying zaleplon including the steps of: dissolving zaleplon sample in acetonitrile:water (1:1) diluent, injecting the sample solution (ca. 10 μl) onto a 100 mm×4 mm, 3 μm RP-18 HPLC column, eluting the sample from the column at 1 ml/min. using a mixture of acetonitrile (28 vol-%) and ammonium-format buffer (72 vol-%, 0.005 M, pH=4) as eluent, and measuring the zaleplon content of the relevant sample at 245 nm wavelength with aUV detector.
The present invention is based on a mechanistic study and new observations concerning the reaction of N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide 3 with 3-amino-4-cyanopyrazole 2 leading to zaleplon. Our observations include identification of a reaction intermediate, imine 6 by high performance liquid chromatography-mass spectroscopy. Our results, including the identification of the imine intermediate, are consistent with a reaction mechanism that is set forth in Scheme 2.
According to Scheme 2, ethylacetamide 3 undergoes Michael-type addition of the 3-amino group of pyrazole 4. a-Elimination of dimethylamine from a transient charge-separated intermediate restores the double bond, which rearranges to form imine intermediate 6. The 2-nitrogen atom of the pyrazole ring cyclizes onto the keto group with elimination of water forming zaleplon.
Both the addition and cyclization reactions occur in the presence of acid. The dimethylamine liberated in the first elimination step binds an equivalent of acid. Consequently an excess of acid is required for this sequence of acid catalyzed conversions to go to completion.
The starting materials, imine intermediate, and product have significantly different polarities. It became apparent during the course of our study that while aqueous mineral acid is a good solvent for both starting materials 3 and 4, it is not a good solvent for imine intermediate 6 or zaleplon. Imine intermediate 3 tends to separate from aqueous mineral acids that do not contain a significant amount of a water-miscible organic co-solvent and forms an oily precipitate, thereby preventing the reaction from going to completion. The starting materials and imine intermediate are soluble in a variety of protic and polar aprotic organic solvents. Unfortunately, the rate of the reaction is solvent dependent and is much slower in the organic solvents we tried than it is in water.
Overcoming the above-mentioned solubility problems, the present invention provides a process for producing zaleplon whereby ethylacetamide 3, or an acid addition salt thereof, is reacted with 3-amino-4-cyanopyrazole 4, or an acid addition salt thereof, in a reaction medium of water and at least one water-miscible organic compound in the presence of an acid. The quantity of water, organic solvent, and acid can be adjusted independently. The water-miscible organic solvent can tend to solubilize imine intermediate 6. As stated previously, an equivalent or more of an acid must be present in order to maintain acidic conditions throughout the course of the reaction. By including at least one water-miscible organic compound, the solvating power in the reaction medium is decoupled from the choice of acid. This flexibility is advantageous because it enables optimization of the production process simultaneously for yield and reaction rate. Such flexibility is not possible in prior art processes. In the process described in the '607 patent, varying the amount of acid is the only means of altering the solvating properties of the reaction medium.
In particular, the reaction medium for production of zaleplon from compounds 3 and 4 according to this invention is a mixture of water and at least one water-miscible organic solvent (organic co-solvent). Organic co-solvents suitable in the practice of the present invention include organic compounds that do not bear carboxylic acid groups, such as C1-C6 monohydroxyl and polyhydroxyl alcohols (e.g. methanol, ethanol, propanol), nitrites (e.g. acetonitrile, propionitrile), ethers (e.g. tetrahydrofuran, dioxane), nitro compounds (e.g. nitromethane, nitroethane), amides (e.g. formamide, dimethylformamide, acetamide, dimethylacetamide, hexamethylphosphoramide and hexamethylphosphortriamide, sulfoxides (e.g. dimethylsulfoxide), and other water-miscible organic compounds that are inert to the reagents and/or the product. Any of the above recited co-solvents can be used alone, or any of them can be used in any combination.
The ratio of organic co-solvent to water in the reaction medium is preferably from about 10% to about 90% (v/v) organic co-solvent in water, more preferably from about 30% to about 40% (v/v) organic co-solvent in water. Most preferably, the reaction medium is a mixture of about 36% (v/v) methanol in water.
As used herein in connection with the composition of water and organic co-solvent in a reaction medium, volume % (vol-%), % v/v, and N % v/v (where N is a number from 1 up to and including 100) are synonymous and calculated as follows (illustrated for species A):
VOl-%A=WtA×ρA/(WtA×ρA+WtB×ρB)
where:
Suitable acids for use in the practice of the method of the present invention include inorganic acids, such as hydrochloric acid, hydrobromic acid, sulfuric acid, phosphoric acid and boric acid, and water-miscible organic acids, such as formic acid, acetic acid, propionic acid, oxalic acid, malonic acid and tartaric acid. The acid should be used in at least an amount capable of protonating all of the liberated dimethylamine, thereby maintaining an at least moderately acidic environment for ring closure of imine intermediate 6 and completion of the zaleplon-forming reaction. An acid may be added individually as such to the reaction mixture. Alternatively, the acid may be added as the proton donating component of an acid addition salt of ethylacetamide 3 or pyrazole 4. Thus, it will be appreciated by those skilled in the art that up to about two equivalents of acid may be added by using acid addition salts of the starting materials. Therefore, separate individual addition of an acid as such is not strictly necessary to establish acidic conditions.
Preferred acids include hydrochloric acid and phosphoric acid, either of which is preferably present in the reaction mixture in an amount of from about one to about two molar equivalents with respect to the limiting reagent. Starting materials 3 and 4 may be used in any ratio. The one present in the lesser molar amount constitutes the limiting reagent to which the amount of acid should be compared. The starting materials are preferably used in approximately equimolar amounts due to their cost.
In accord with especially preferred sets of production parameters the reaction goes to completion within several hours at ambient temperature, without external heating or cooling. The process according to the present invention is preferably conducted at a temperature in the range of from about 20° C. to about 25° C. The reaction also may be conducted at elevated temperature, up to the boiling point of the reaction medium (e.g. Examples 16-18), as well as at lower temperatures (e.g. Example 21).
The reaction time necessary for complete conversion is about 2 to about 8 hours at a temperature in the range of from about 20° C. to about 25° C., depending upon the composition of the reaction mixture. The time required for the reaction to go to completion may be decreased to about 0.2 hours at an elevated temperature of about 50° C. Reactions performed with cooling require more time to reach completion (about 6 to about 8 hours) but yield a product of somewhat higher purity (compare Examples 13 and 21).
By following the preferred embodiments of the invention, the zaleplon product precipitates from the reaction mixture by the end of the reaction or may be induced to precipitate by cooling. The precipitate may be recovered by filtration. Cooling the reaction mixture before collecting the product may increase the yield.
This process produces pure N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-7-yl)phenyl]-N-ethylacetamide (zaleplon) in the highest yield currently reported. The process of this invention achieves a higher reaction rate at lower temperatures than is possible using known processes for producing zaleplon.
The purity of the product, as isolated, is very high (above 98.5%). However, if desired, pure zaleplon obtained by the process of the present invention and having a purity of at least 98.5%, preferably at least 99%, as determined by HPLC, can be recrystallized from a solvent, preferably from methanol, ethanol, or a reaction medium of water and a co-solvent such as methanol, ethanol, acetonitrile and the like in order to produce a drug substance that complies with regulatory requirements.
The present invention provides a process that is especially adapted for increasing the purity of a crude zaleplon that can be in mixture with zaleplon regioisomer and other impurities. The present invention also provides a process for enriching such mixtures in regioisomer (5), thereby facilitating the isolation of regioisomer in yet another embodiment of the present invention.
Crude zaleplon useful in the several embodiments of the present invention may be provided as a condensed, unpurified or partially purified end product of a chemical synthesis such as those described in U.S. Pat. Nos. 4,626,538, 5,714,607 and U.S. patent application Ser. No. 10/170,673, or from any source.
The compound N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-5-yl)phenyl]-N-ethylacetamide (5), regioisomer of zaleplon, has been discovered as a main impurity in the synthesis of zaleplon starting from 3-amino-4-cyanopyrazole and N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide. Under the reaction conditions disclosed in the U.S. patent application Publication No. 2003/0040522, the amount of the regioisomer impurity is about 0.2-0.5% (HPLC) in the crude product. The amount of this impurity is strongly dependent on the reaction conditions and, as described hereinbelow, the reaction conditions can be manipulated to maximize the amount of regioisomer formed, thereby facilitating its isolation and characterization.
Thus, in another embodiment, the present invention provides a method for the preparation of the novel N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-5-yl)phenyl]-N-ethylacetamide (5) starting from 3-amino-4-cyanopyrazole and N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide by reacting them in the presence of an acid in water or in a mixture of water and a water miscible organic solvent in the presence of an acid. The amount of regioisomer (5) can be increased up to 5% (HPLC) by use of a high concentration of a strong acid in the synthesis. This facilitates the isolation and characterization of this new compound.
The reaction can be performed at 20° to 30° C., or at higher temperature up to the boiling point of water. A temperature of 20° to 30° C. is preferred. As a water miscible organic solvent both polar protic (e.g. acetic acid, methanol, ethanol, i-propanol) or polar aprotic (e.g. acetonitrile, tetrahydrofuran, dimethylformamide) solvents can be used. As acid, both mineral (e.g. hydrochloric, sulfuric, phosphoric) and organic (e.g. acetic, trifluoroacetic, methanesulfonic) can be used. Hydrochloric acid is the preferred acid.
In a preferred embodiment, the reaction is performed in water in the presence of hydrochloric acid at about 25° C. Isolation of the mixture of zaleplon and its regioisomer (5) can be performed by evaporation, filtration, extraction or by any combination of these methods.
In a particularly preferred embodiment, after completion of the reaction, the reaction mixture is diluted with water and the precipitated zaleplon is removed by filtration. Then the filtrate is neutralized to precipitate the mixture of zaleplon and its regioisomer 5. A further crop of the mixture can be obtained by extraction of water phase with water immiscible organic solvents such as ethylacetate, dichloromethane, chloroform and like.
Isolation of compound 5 can be performed by chromatography. Column chromatography, preparative TLC or HPLC can be applied. Column chromatography is preferred. As a packing, silica gel or aluminium oxide can be used. Silica gel is the preferred packing. As eluent, various organic solvents or mixtures of them can be used. Mixtures of dichloromethane and acetone are preferred as column eluent. A 3:1 (v:v) mixture of dichloromethane:acetone is particularly preferred as eluent.
Isolated 5 was characterized, and its structure proved, by 1H-NMR and 13C-NMR spectroscopy, as well as by mass spectrometric investigations.
13C resonance assignments
In a further embodiment, the present invention provides novel HPLC methods for determination of the impurity profile and assay of zaleplon.
In one such embodiment, suitable for complete resolution (separation) of the peak of zaleplon (1) from the peak of structurally very similar compound (5) as well as the other impurities, the present invention provides a method for HPLC including the steps of:
In another embodiment, particularly suitable for analysis and assay of zaleplon and its main impurity 5 in a drug substance and pharmaceutical compositions containing zaleplon, the present invention provides an HPLC method including the steps of:
accordance with another embodiment of the invention, zaleplon is purified by precipitation under controlled conditions from a solution prepared from a crude zaleplon than can contain zaleplon regioisomer. Impure zaleplon may be subjected to a single iteration of the process to obtain more highly pure zaleplon or the process may be repeated to obtain zaleplon in any desired accessible purity level, including zaleplon essentially free of regioisomer.
In the purification process of the present invention, a solid enriched in zaleplon is precipitated from a solution including an organic solvent. Organic solvents include alcohols, such as methanol, ethanol and 2-propanol; ketones, such as acetone, methyl ethyl ketone and methyl isobutyl ketone; ethers, such as tetrahydrofuran (THF), diethyl ether and methyl t-butyl ether; carboxylic acids, such as acetic acid and propionic acid; carboxylic acid esters, such as ethyl acetate and isobutyl acetate; nitriles, such as acetonitrile and acrylonitrile; aromatic hydrocarbons, such as benzene, toluene and xylenes and halogenated hydrocarbons, such as dichloromethane and chloroform, and mixtures thereof. Optionally, water can be combined with the organic solvent. It will be understood that the organic solvent is selected with reference to its freezing point and the temperature(s) at which the process is performed so that the solvent will not freeze. Generally, preferred organic solvents are acetic acid, methanol, ethanol, 2-propanol, tetrahydrofuran (THF), acetonitrile, acetone, ethyl acetate, toluene and dichloromethane.
The optimal concentration of zaleplon in the solution generally is in a range of from about 100 mM to about 1M, more preferably from about 100 mM to about 700 mM. The organic solvent may be heated to an elevated temperature to obtain a homogeneous solution of the crude zaleplon mixture. As used herein, the term “elevated temperature” means a temperature above about 25° C. Using an organic solvent that boils at the desired temperature is a matter of convenience. Solutions saturated with zaleplon at the temperature at which the solution is formed tend to separate zaleplon from regioisomer 5 as effectively as unsaturated solutions. Forming a saturated solution is preferred.
After the crude zaleplon has completely dissolved, precipitation of a solid enriched in zaleplon from the solution can be induced by cooling. Cooling includes both active cooling by placing an external heat sink where heat exchange can occur between the solution and the heat sink or passive cooling by cessation of active heating. Preferably, the solution is cooled to a reduced temperature, more preferably, to about 5-10° C. Precipitation can also be induced with the aid of an antisolvent, optionally with cooling. As used herein, the term “reduced temperature” means a temperature below about 20° C.
Cooling causes precipitation of a solid enriched in zaleplon relative to the crude zaleplon/regioisomer mixture.
After precipitating the solid enriched in zaleplon from the solution, the solid is separated from the solution depleted of zaleplon to obtain purified zaleplon. Separating can be by any conventional technique for removing a solid from a liquid, such as by filtering or decanting. Further, separating optionally includes conventional washing and drying of the solid, such as is illustrated in the examples.
In one embodiment of the purification process, an antisolvent is added to the solution. An antisolvent, as that term is used in this disclosure, means any liquid in which zaleplon is no more than sparingly soluble and which does not form a separate liquid phase during the process. Preferred antisolvents include aliphatic hydrocarbons and water, with pentane, hexane, heptane, octane, petroleum ether and water being more preferred, hexane and water being most preferred. The ratio of antisolvent to organic solvent is preferably from about 1:1 to about 4:1, more preferably about 1:1 to about 2:1.
When an aliphatic hydrocarbon antisolvent is used, preferred organic solvents are acetic acid, methanol, ethanol, 2-propanol, THF, acetonitrile, acetone, ethyl acetate, toluene and dichloromethane. Preferred organic solvents when the antisolvent is water are acetic acid, methanol, ethanol, 2-propanol, THF, acetonitrile and acetone.
When using an antisolvent, it is preferable to work at a lower concentration range. The preferred concentration range of zaleplon in the organic solvent when an antisolvent is to be added is from about 100 mM to about 400 mM. The antisolvent is preferably added to the solution before the appearance of cloudiness or a precipitate, more preferably the antisolvent is added at elevated temperature.
The antisolvent can be used to assist in forming a saturated or nearly saturated solution without having to remove excess undissolved solids. An unsaturated solution of zaleplon and the regioisomer is formed in the organic solvent. The antisolvent is added to the solution until zaleplon begins to precipitate. Then, the temperature is increased and/or additional organic solvent is added until the precipitated zaleplon goes into solution again, and the purification process is continued by precipitating zaleplon from the so-formed solution.
In especially preferred embodiments, a single iteration of the purification process can reduce the regioisomer content of a crude zaleplon by 50% or more, and even 70% or more. Such reduction is highly effective considering the structural similarity between zaleplon and regioisomer 5. A single iteration of the purification process can reduce the proportion of regioisomer from a value of about 0.2% in crude zaleplon to about 0.03% in solid enriched zaleplon, which amounts to removal of 84% of the regioisomer. Further reduction in the amount of the regioisomer can be achieved by repeating the purification process.
Using an antisolvent can increase the recovery of zaleplon without substantially diminishing the degree of the separation. As demonstrated in the Examples, using an antisolvent in combination with a representative selection of organic solvents uniformly increased recovery of zaleplon.
By means of the purification process of the invention, zaleplon with less than 0.033% regioisomer (according to the HPLC method of the present invention) can be obtained.
Thus, in another embodiment the present invention provides zaleplon having a purity of at least about 98.5% and most preferably at least about 99%. As used herein, percent purity refers to area percent purity determined by the HPLC method herein described. Thus zaleplon of 99% purity (or 99% pure zaleplon) means that the ratio of the HPLC peak area for zaleplon to the sum of all HPLC peak areas, times 100, is 99.
Some embodiments of the purification process were found to produce novel crystalline forms of zaleplon. The stepwise procedure of the purification process can be used to prepare the new forms from pure or impure zaleplon. The new forms also may be accessible by any number of other techniques arrived at empirically.
The new forms are distinguishable from the zaleplon that is available in Sonata® by characteristics of their X-ray diffraction patterns. The zaleplon that is in Sonata® is designated Form I in this disclosure. Zaleplon Form I has characteristic peaks in its powder X-ray diffraction pattern (
Zaleplon Form II can be prepared following the stepwise procedure of the purification process by using ice water as an antisolvent and a water-miscible or substantially water soluble organic solvent. In particular, zaleplon Form II may be prepared by dissolving zaleplon in a substantially water soluble or water-miscible organic solvent selected from among those previously described. Preferred organic solvents for producing Form II zaleplon are acetic acid, methanol, ethanol, 2-propanol, THF, acetonitrile and acetone. Zaleplon Form II can be precipitated at any temperature, but the temperature is conveniently ambient or elevated. To optimize the recovery of zaleplon, it is preferred to saturate the organic solvent with zaleplon at elevated temperature. Ice water is then added to the mixture. The ratio of the organic solvent and ice water can be from about 1:2 to about 1:5 (v/v), with about 1:3 (v/v) being preferred. Although adding ice water will cool the mixture, the organic solvent/water mixture preferably is further cooled to about 5-10° C. if necessary. The mixture should be stirred while water is added and the mixture is cooled. Under the preferred conditions, crystallization of Form II is substantially complete in about an hour or less, whereupon it can be separated, including optional washing and drying, to obtain crystalline zaleplon Form II.
Zaleplon Form II is characterized by a powder X-ray diffraction pattern (
Zaleplon Form III can be prepared by dissolving zaleplon in refluxing acetonitrile, adding water to the refluxing solution in an amount of from about 2:1 (v/v) to about 4:1 (v/v), preferably about 3:1 (v/v), relative to the acetonitrile, and cooling the mixture to about 5-10° C. without stirring.
Zaleplon Form III was characterized by PXRD spectroscopy and was found to have characteristic peaks in the diffraction pattern (
Zaleplon Form III is further characterized by peaks in the x-ray diffraction at 11.6, 17.6, 19.0, 20.0, and 22.2±0.2 degrees two-theta.
A novel crystalline form of zaleplon designated Form IV can be prepared by forming a solution of zaleplon in a 1:1 (v/v) mixture of water and THF at reflux, and cooling the solution to room temperature without stirring. Separating the precipitated solid yields zaleplon Form IV. Form IV also can be prepared by forming a solution of zaleplon in 2-propanol at reflux, cooling the solution to 5-10° C. without stirring and separating the precipitated solid.
Zaleplon Form IV was characterized by PXRD spectroscopy and was found to have characteristic peaks in the diffraction pattern (
Zaleplon Form IV can be further characterized by peaks in the x-ray diffraction diagram at 10.6, 11.1, 14.1, 15.6, 18.0, 18.2, 20.1, 20.3, 24.3, 25.0, 25.9, 26.7, 27.9, and 29.5±0.2 degrees two-theta.
Yet another novel crystalline form of zaleplon, Form V, is obtained by following the Examples in U.S. patent application Ser. No.10/170,673 which has been incorporated by reference in its entirety.
Zaleplon Form V was characterized by PXRD spectroscopy and was found to have characteristic peaks in the diffraction pattern (
Zaleplon Form V can be further characterized by x-ray diffraction peaks at 10.7, 11.0, 12.5, 15.4, 16.5, 17.7, 21.3, 25.7, and 26.5±0.2 degrees two-theta.
The invention further provides novel processes for preparing known zaleplon Form I. In one process for making crystalline zaleplon Form I, zaleplon is suspended in water and refluxed. The suspension is then cooled to room temperature. The crystals are filtered and dried to yield crystalline zaleplon Form I.
According to another process for making zaleplon Form I, zaleplon is slurried in high boiling hydrocarbons. Hydrocarbons are selected from toluene, xylenes, tetrahydronaphthalene and the like. A suitable temperature can be a temperature from about 100° C. to the melting point of zaleplon. After treatment at high temperature the suspension is then cooled to room temperature. The crystals are filtered and dried to yield crystalline zaleplon Form I.
According to another embodiment of the process for making zaleplon Form I, zaleplon is melted and the melted zaleplon is cooled to room temperature and ground to yield crystalline zaleplon Form I.
Novel zaleplon Form II, III, IV and V are useful for delivering zaleplon to the gastrointestinal tract, mucus membranes and circulatory system of a patient suffering from insomnia. They can be formulated into a pharmaceutical product like Sonata® or another dosage form.
Pharmaceutical compositions of the present invention contain zaleplon Forms II, III, IV and V, optionally in mixture with other forms or amorphous zaleplon and/or other active ingredients. In addition to the active ingredient(s), the pharmaceutical compositions of the present invention may contain one or more excipients. Excipients are added to the composition for a variety of purposes.
Diluents increase the bulk of a solid pharmaceutical composition and may make a pharmaceutical dosage frown containing the composition easier for the patient and caregiver to handle. Diluents for solid compositions include, for example, microcrystalline cellulose (e.g. Avicel®), microfine cellulose, lactose, starch, pregelitinized starch, calcium carbonate, calcium sulfate, sugar, dextrates, dextrin, dextrose, dibasic calcium phosphate dihydrate, tribasic calcium phosphate, kaolin, magnesium carbonate, magnesium oxide, maltodextrin, mannitol, polymethacrylates (e.g. Eudragit®), potassium chloride, powdered cellulose, sodium chloride, sorbitol and talc.
Solid pharmaceutical compositions that are compacted into a dosage form like a tablet may include excipients whose functions include helping to bind the active ingredient and other excipients together after compression. Binders for solid pharmaceutical compositions include acacia, alginic acid, carbomer (e.g. carbopol), carboxymethylcellulose sodium, dextrin, ethyl cellulose, gelatin, guar gum, hydrogenated vegetable oil, hydroxyethyl cellulose, hydroxypropyl cellulose (e.g. Klucel®), hydroxypropyl methyl cellulose (e.g. Methocel®), liquid glucose, magnesium aluminum silicate, maltodextrin, methylcellulose, polymethacrylates, povidone (e.g. Kollidon®, Plasdone®), pregelatinized starch, sodium alginate and starch.
The dissolution rate of a compacted solid phanmaceutical composition in the patient's stomach may be increased by the addition of a disintegrant to the composition. Disintegrants include alginic acid, carboxymethylcellulose calcium, carboxymethylcellulose sodium (e.g. Ac-Di-Sol®, Primellose®), colloidal silicon dioxide, croscarmellose sodium, crospovidone (e.g. Kollidon®, Polyplasdone®), guar gum, magnesium aluminum silicate, methyl cellulose, microcrystalline cellulose, polacrilin potassium, powdered cellulose, pregelatinized starch, sodium alginate, sodium starch glycolate (e.g. Explotab®) and starch.
Glidants can be added to improve the flow properties of non-compacted solid composition and improve the accuracy of dosing. Excipients that may function as glidants include colloidal silicon dioxide, magnesium trisilicate, powdered cellulose, starch, talc and tribasic calcium phosphate.
When a dosage form such as a tablet is made by compaction of a powdered composition, the composition is subjected to pressure from. punches and a die. Some excipients and active ingredients have a tendency to adhere to the surfaces of the punch and die, which can cause the product to have pitting and other surface irregularities. A lubricant can be added to the composition to reduce adhesion and ease release of the product from the die. Lubricants include magnesium stearate, calcium stearate, glyceryl monostearate, glyceryl palmitostearate, hydrogenated castor oil, hydrogenated vegetable oil, mineral oil, polyethylene glycol, sodium benzoate, sodium lauryl sulfate, sodium stearyl fumarate, stearic acid, talc and zinc stearate.
Flavoring agents and flavor enhancers make the dosage form more palatable to the patient. Common flavoring agents and flavor enhancers for pharmaceutical products that may be included in the composition of the present invention include maltol, vanillin, ethyl vanillin, menthol, citric acid, fumaric acid, ethyl maltol, and tartaric acid.
Solid and liquid compositions also may be dyed using any pharmaceutically acceptable colorant to improve their appearance and/or facilitate patient identification of the product or unit dosage level.
In liquid pharmaceutical compositions of the present invention, Forms II, III, IV and V and any other solid excipients are dissolved or suspended in a liquid carrier such as water, vegetable oil, alcohol, polyethylene glycol, propylene glycol or glycerin.
Liquid pharmaceutical compositions may contain emulsifying agents to disperse uniformly throughout the composition an active ingredient or other excipient that is not soluble in the liquid carrier. Emulsifying agents that may be useful in liquid compositions of the present invention include, for example, gelatin, egg yolk, casein, cholesterol, acacia, tragacanth, chondrus, pectin, methyl cellulose, carbomer, cetostearyl alcohol and cetyl alcohol.
Liquid pharmaceutical compositions of the present invention also may contain a viscosity enhancing agent to improve the mouth-feel of the product and/or coat the lining of the gastrointestinal tract. Such agents include acacia, alginic acid bentonite, carbomer, carboxymethylcellulose calcium or sodium, cetostearyl alcohol, methyl cellulose, ethylcellulose, gelatin guar gum, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropyl methyl cellulose, maltodextrin, polyvinyl alcohol, povidone, propylene carbonate, propylene glycol alginate, sodium alginate, sodium starch glycolate, starch tragacanth and xanthan gum.
Sweetening agents such as sorbitol, saccharin, sodium saccharin, sucrose, aspartame, fructose, mannitol and invert sugar may be added to improve the taste.
Preservatives and chelating agents such as alcohol, sodium benzoate, butylated hydroxy toluene, butylated hydroxyanisole and ethylenediamine tetraacetic acid may be added at levels safe for ingestion to improve storage stability.
A liquid composition according to the present invention also may contain a buffer such as guconic acid, lactic acid, citric acid or acetic acid, sodium guconate, sodium lactate, sodium citrate or sodium acetate.
Selection of excipients and the amounts to use may be readily determined by the formulation scientist based upon experience and consideration of standard procedures and reference works in the field.
The solid compositions of the present invention include powders, granulates, aggregates and compacted compositions. The dosages include dosages suitable for oral, buccal, rectal, parenteral (including subcutaneous, intramuscular, and intravenous), inhalant and ophthalmic administration. Although the most suitable route in any given case will depend on the nature and severity of the condition being treated, the most preferred route of the present invention is oral. The dosages may be conveniently presented in unit dosage form and prepared by any of the methods well-known in the pharmaceutical arts.
Dosage forms include solid dosage forms like tablets, powders, capsules, suppositories, sachets, troches and losenges as well as liquid syrups, suspensions and elixirs.
The active ingredient and excipients may be formulated into compositions and dosage forms according to methods known in the art.
Capsules, tablets and lozenges and other solid unit dosage forms preferably contain a dosage level of from about 5 to about 20 mg, more preferably from about 5 mg to about 10 mg of zaleplon.
In yet another embodiment, the present invention provides novel gradient elution HPLC method for determination of the impurity profile zaleplon, that is for quantifying, by area percent, the amounts of impurities present in a sample of zaleplon. In this embodiment, suitable for complete resolution (separation) of the peak of zaleplon (1) from the peak of structurally very similar compound (5), as well as from r the other impurities, the present invention provides a HPLC method including the steps of:
c, gradient eluting at 1 ml/min. with a mixture of acetonitrile (A) and ammonium-formate buffer (B, 0.005 M, pH=4) according to the following profile:
In the above method, zaleplon has a retention time of about 17 minutes. A typical HPLC chromatogram using this method is shown in
In another embodiment, adapted to assay of zaleplon and its main impurity 5 in a drug substance and pharmaceutical compositions containing zaleplon, the present invention provides an isocratic HPLC assay method including the steps of:
In this method, zaleplon has a retention time of about 5 min.
Having thus described the various aspects of the present invention, the following non-limiting examples are provided to illustrate specific embodiments.
General
Ethylacetamide 3 was used as received from Precise Chemipharma PVT. Ltd. 3-Amino-4-cyanopyrazole 4 was used as received from Precise Chemipharma PVT. Ltd. Phosphoric acid (85%) was used as received from Aldrich Chemical Co. Organic solvents and antisolvents were used as received.
Zaleplon and regioisomer 5 in the crude zaleplon (i.e. starting mixture) and precipitated products were quantitated by HPLC using UV detection at a wavelength of 254 nm, at which wavelength the response factor of zaleplon and its regioisomer 5 are the same.
Carbon-13 NMR spectra and proton NMR spectra were obtained at 125 MHz and 500 MHz, respectively, using a Brucker Model DRX spectrometer. The temperature of measurement was 27° C.
Low resolution EI mass spectra were obtained with a VG-7035 mass spectrometer (VG Analytical, Manchester, England). The ionization energy was 70 eV, the ion current was 200 μA. The source temperature was 150°. Theoretical MW=305.127; m/Z found=305.128.
Ethylacetamide 3 (260 g, 1 mol) and 3-amino-4-cyanopyrazole 4 (108 g, 1 mol) were dissolved in a mixture of water (7 L) and ethanol (4 L). Eighty five percent aqueous phosphoric acid (67 ml, 1 mol) was added and the mixture was stirred at room temperature for 8 h. The reaction mixture was then cooled to 5° C. and the crystalline product that formed was collected, washed with water and dried at 60° C. to afford zaleplon (275 g, 90.2%) which was 99.36 pure by HPLC and contained 0.21% regioisomer 5.
The mixture of zaleplon and regioisomer 5 prepared in Preparation 1 (4 g) was dissolved in refluxing organic solvent. After the zaleplon was completely dissolved, the solution was allowed to cool to room temperature and then was further cooled to 6° C. and maintained at that temperature for 1 day. The resulting crystalline solid was recovered by filtration, washed with the fresh chilled organic solvent from which it was precipitated and dried at 60° C. under vacuum. The separation acheived using different organic solvents is recorded in Table 1.
The mixture of zaleplon and regioisomer 5 prepared in Preparation 1 (4 g) was dissolved in refluxing organic solvent. After the zaleplon had completely dissolved, antisolvent was slowly added to the refluxing solution. After completing the addition, the mixture was cooled to 5° C. The resulting crystalline solid was recovered by filtration washed with fresh chilled organic solvent from which it was precipitated and dried under vacuum at 60° C. The separation acheived using different organic solvent and antisolvent combinations is recorded in Table 2.
Zaleplon (10 g) was dissolved in refluxing ethanol (100 ml) with stirring. Hexane (200 ml) was added dropwise to the refluxing solution. Then, the mixture was cooled to 5° C. with stirring over about 4 h. The precipitate was collected by filtration to yield crystalline zaleplon Form I (8.9 g, 89%).
Zaleplon (10 g) was dissolved in acetic acid (50 ml) at 50° C. with stirring. The resulting solution was poured into ice-water (150 ml) to induce immediate precipitation.
The precipitate was collected by filtration to yield crystalline zaleplon Form II (8.5 g, 85 %)
Zaleplon (10 g) was dissolved in refluxing acetonitrile (50 ml) with stirring. Water (150 ml) was added dropwise to the refluxing solution. Then, the clear solution was cooled to 5° C. without stirring. The precipitate was collected by filtration to yield crystalline zaleplon form III (9.1 g, 91%).
Zaleplon (10 g) was dissolved in refluxing 2-propanol (150 ml) with stirring. The clear solution was cooled to 5° C. without stirring. The precipitate was collected by filtration to yield crystalline zaleplon form IV (8.6 g, 86%).
Zaleplon (26.8 g) is dissolved in the mixture of ethanol and water (210 and 210 cm3) at reflux temperature then treated with charcoal (2.7 g, 10 m/m%). The solution is stirred for 30 minutes at reflux temperature and filtered. The charcoal is washed with a hot mixture of ethanol and water (30:30 cm3). The solution is cooled to 25° C. in 6 hours and kept at this temperature for 2 hours. Crystals are filtered and washed with the mixture of ethanol and water (20:20 cm3) and dried under vacuum at 60° C. for 8 hours to afford crystalline zaleplon form I (22. 8 g, 85%)
Zaleplon (22.8 g) is dissolved in ethanol (230 cm3) at reflux temperature then treated with charcoal (2.3 g, 10 m/m%). The solution is stirred for 10 minutes and filtered. The charcoal is washed with hot ethanol (20 cm3). The solution is cooled to 25° C. in 6 hours and kept at this temperature for 2 hours. Crystals are filtered and washed with ethanol (30 cm3). The product is dried under vacuum at 60° C. for 8 hours to afford zaleplon form I (18.7 g, 82%).
N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide (5.2 g, 0.02 mol) and 3-amino-4-cyanopyrazole (2.16 g, 0.02 mol) were dissolved in the mixture of water (50 ml) and concentrated hydrochloric acid (40 ml) and the mixture was stirred at room temperature for 8 h. The reaction mixture was then cooled to 5° C. and the precipitate was removed by filtration. The filtrate was neutralized by concentrated aqueous ammonia solution to precipitate 380 mg of the mixture of zaleplon and its regioisomer 5 which was collected by filtration. The filtrate was extracted with 100 ml of ethylacetate to give 100 mg of the mixture of the above two compounds upon evaporation. The two crops combined were put to a silica gel column (100 g) and the elution was performed by the solvent mixture of chloroform and acetone 3:1 (v/v) to yield as a second crop 240 mg (4%) of 5; mp 194-196° C.; 1H-NMR (CDCl3) δ (ppm) 1.143 (t, 3H), 1.876 (s, 3H), 3.804 (q, 2H), 7.361 (d, 1H), 7.532 (d, 1H), 7.613 (t, 1H), 8.018 (s, 1H), 8.159 (d, 1H), 8.375 (s, 1H), 8.805 ((d, 1H); 13C-NMR (CDCl3) δ (ppm) 12.89, 22.68, 43.84, 83.17, 107.71, 112.84, 127.17, 127.48, 130.62, 131.63, 136.67, 137.46, 144.10, 148.31, 149.99, 158.60, 169.90; MS (EI, 70 EV) m/z (%) 305 (M+, 18), 248 (59).
Crude zaleplon prepared as in Preparation 1 (4 g) is dissolved in refluxing acetonitrile (20 mL). When the zaleplon is completely dissolved, the solution is allowed to cool to a temperature between about 20° C. and about 25° C. The resulting mixture is then cooled to about 6° C. and maintained at that temperature for about 24 hours. The precipitate that is a solid enriched in zaleplon is recovered by filtration and washed with fresh chilled acetonitrile.
The recovered precipitate of solid enriched in zaleplon (ca. 2.3 g) is dissolved in refluxing acetonitrille (ca. 10 mL). The solution is allowed to cool to a temperature between about 20° C. and about 250° C. The resulting mixture is then cooled to about 6° C. and maintained at that temperature for about 24 hours. The precipitate is recovered by filtration, washed with fresh chilled acetonitrile, and dried at 60° C. under vacuum. The recovered precipitate of further purified Zaleplon is analyzed by the gradient HPLC method of the present invention and found to be >99% pure. No regioisomer is detected in the precipitate using the gradient HPLC method of the present invention. The zaleplon is essentially free of regioisomer.
N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide (2.6 g, 0.01 mol) and 3-amino-4-cyanopyrazole (1.08 g, 0.01 mol) were dissolved in the mixture of water (35 cm3) and methanol (20 cm3). Phosphoric acid (85%) (0.67 cm3, 0.01 mol) was then added and the mixture was stirred at room temperature for about 4 hours. The reaction mixture was then cooled to about 5° C. and the crystalline product that formed was collected, washed with water and dried at about 60° C. to yield zaleplon (2.79 g, 91.5%) in 98.83% purity as determined by HPLC.
N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide (2.6 g, 0.01 mol) and 3-amino-4-cyanopyrazole (1.08 g, 0.01 mol) were dissolved in the mixture of water (35 cm3) and ethanol (20 cm3). Phosphoric acid (85%) (0.67 cm3, 0.01 mol) was then added and the mixture was stirred at room temperature for about 8 hours. The reaction mixture was then cooled to about 5° C. and the crystalline product that formed was collected, washed with water and dried at about 60° C. to yield zaleplon (2.95 g, 96.7%) in 99.09% purity as determined by HPLC.
N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide (2.6 g, 0.01 mol) and 3-amino-4-cyanopyrazole (1.08 g, 0.01 mol) were dissolved in the mixture of water (35 cm3) and methanol (20 cm3). Concentrated (37%) hydrochloride acid (1.0 cm3, 0.012 mol) was then added and the mixture was stirred at room temperature for about 2 hours. The reaction mixture was then cooled to about 5° C. and the crystalline product that formed was collected, washed with water and dried at about 60° C. to yield zaleplon (2.80 g, 91.8%) in 98.69% purity as determined by HPLC.
aDetermined as percent area of the peak corresponding to zaleplon in an HPLC chromatogram of the crude reaction mixture.
N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide (26.0 g, 0.1 mol) and 3-amino-4-cyanopyrazole (10.8 g, 0.1 mol) were dissolved in the mixture of water (350 cm3) and methanol (200 cm3). Concentrated (37%) hydrochloric acid (12.5 cm3, 0.12 mol) was then added and the mixture was stirred at room temperature for about 2 hours. The reaction mixture was then cooled to about 5° C. and the crystalline product formed was collected, washed with water and dried at about 60° C. to yield zaleplon (29.8 g, 97.7%) in 99.08% purity as determined by HPLC.
N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide (2.6 g, 0.01 mol) and 3-amino-4-cyanopyrazole-hydrochloride (1.44 g, 0.01 mol) were dissolved in the mixture of water (35 cm3) and methanol (20 cm3). Concentrated (37%) hydrochloric acid (0.83 cm3, 0.01 mol) was then added and the mixture was stirred at room temperature for about 2 hours. The reaction mixture was then cooled to about 5° C. and the crystalline product formed was collected, washed with water and dried at about 60° C. to yield zaleplon (2.93 g, 96.1%) in 99.16% purity as determined by HPLC.
N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide (2.6 g, 0.01 mol) and 3-amino-4-cyanopyrazole (1.08 g, 0.01 mol) were dissolved in the mixture of water (35 cm3) and methanol (20 cm3). Concentrated (37%) hydrochloric acid (1.25 cm, 0.015 mol) was then added and the mixture was stirred at about 15° C. for about 8 hours. The reaction mixture was then cooled to about 5° C. and the crystalline product formed was collected, washed with water and dried at about 60° C. to yield zaleplon (2.87 g, 94.1%) in 99.5% purity as determined by HPLC.
This application is a continuation-in-part of U.S. patent application Ser. No. 10/170,673, filed Jun. 12, 2002, which claims the benefit of U.S. Provisional Application Ser. No. 60/297,635, filed Jun. 12, 2001. This application is also a continuation-in-part of U.S. patent application Ser. No. 10/211,461, filed Aug. 1, 2002, which claims the benefit of U.S. Provisional Application Ser. No. 60/309,391, filed Aug. 1, 2001; U.S. Provisional Application Ser. No. 60/317,907, filed Sep. 6, 2001; and U.S. Provisional Application Ser. No. 60/388,199, filed Jun. 12, 2002. All of these applications are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 60297635 | Jun 2001 | US | |
| 60309391 | Aug 2001 | US | |
| 60317907 | Sep 2001 | US | |
| 60388199 | Jun 2002 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 10170673 | Jun 2002 | US |
| Child | 10874907 | Jun 2004 | US |
| Parent | 10211461 | Aug 2002 | US |
| Child | 10874907 | Jun 2004 | US |
