HK1064671B - Process for making amlodipine maleate, the amlodipine maleate prepared, the pharmaceutical composition and the use thereof - Google Patents

Description

Process for preparing amlodipine maleate, prepared amlodipine maleate, pharmaceutical composition and use thereof

The invention relates to a process flow for preparing high-purity amlodipine maleate.

Calcium channel blockers (calcium antagonists) are useful in the treatment of heart diseases including angina pectoris and/or hypertension. Dihydropyridine dicarboxylate derivatives are generally considered to have calcium channel blocking activity. For example, patent EP 089167 and its corresponding US 4,572,909 disclose a group of 2-amino-group-containing-3, 5-dicarboxylate dihydropyridine derivatives as effective calcium channel blockers. One of the compounds considered to be the most preferred by these patents is 2- [ (2-aminoethoxy) methyl ] -4- (2-chlorophenyl) -3-ethoxycarbonyl-5-methoxycarbonyl-6-methyl-1, 4-dihydropyridine. The compound is the amlodipine which is well known at present, and the structural formula of the compound is as follows:

amlodipine exhibits good bioavailability in vivo and has a long half-life. A series of suitable acid addition salts are mentioned in these patents, but of these maleic acid salts are considered to be the best one. EP89167, examples 9, 11, 12 and 22 and j.med.chem.29, 1698(1986) disclose a process for the preparation of amlodipine maleate (1: 1 molar ratio of the two components) by dissolving a reaction mixture containing a crude in situ prepared amlodipine base in ethyl acetate or ethanol and adding solid maleic acid, whereupon amlodipine maleate precipitates. This salt is isolated by filtration and recrystallization from ethyl acetate or acetone/ethyl acetate 1: 1 mixtures.

However, commercial amlodipine products (NORVASC from Pfizer, norvas a) employ amlodipine besylate (benzene sulfonate salt) instead of amlodipine maleate. Indeed, the latter patent EP 244944 and its corresponding US 4,879,303 indicate that benzenesulfonates have certain advantages over other known salts, including good formulation properties. It is clear that amlodipine maleate has eventually shifted to amlodipine besylate as it encounters tabletting and stability problems during development. [ see "Review of organic NDA" NDA #19-787, available from FDA under the < information free methods > (FOIA) 10 months and 10 days 1990 ]. Stability and tableting problems are not disclosed in the FDA-derived data.

The present invention relates to the discovery of a previously unpublished impurity accompanying amlodipine maleate and a process that avoids its formation during production. In particular, the present invention relates to a process which comprises reacting amlodipine or a pharmaceutically acceptable salt thereof with maleic acid in an acidic environment to form an amlodipine maleate product. The process uniquely relates to the production of amlodipine maleate which is substantially free of amlodipine aspartate byproduct comprising the steps of: (a) or (1) adding the amlodipine source to the maleic acid solution or suspension in a continuous or intermittent dosing manner to form a solution wherein the relative molar ratio of maleic acid to added amlodipine is at least 1.01: 1, or (2) contacting the amlodipine source with the maleic acid solution or suspension in a continuous or intermittent manner under pH control to form a solution wherein the pH of the solution is no more than 6.5; and (b) isolating amlodipine maleate as a solid from the solution. The invention further relates to a process for the purification of amlodipine maleate, comprising crystallizing or precipitating amlodipine maleate from said solution containing excess maleic acid.

FIG. 1 shows an infrared spectrum of the substance in example 1

FIG. 2 shows the Differential Scanning Calorimetry (DSC) curve of the material of example 1

FIG. 3 shows the X-ray diffraction pattern of the substance of example 1

Although the conversion of amlodipine free base or salt to amlodipine maleate is substantially simple, it has been found that known procedures for preparing amlodipine maleate can result in the formation of a large number of by-products having the formula (1):

the compound of structural formula (1), hereinafter referred to as "amlodipine aspartate", is a by-product accompanied only by maleate salt of amlodipine, which is produced by Michael addition reaction of the amino group of amlodipine with the double bond on maleic acid.

It has now been found that the production schemes described in the above patents and literature may produce only negligible amounts of amlodipine aspartate byproduct on a laboratory scale, but that this byproduct may increase substantially under scale-up production conditions, i.e. temperature conditions need to be intensified in order to drive the conversion to completion and obtain a good crystalline form of amlodipine maleate.

Any substance intended for administration to a patient as a therapeutic agent is generally undesirable for the presence of by-products. Removal of by-products and impurities can increase production costs and reduce yields due to material losses during the purification step. It is therefore advantageous to control the production of by-products and impurities as little as possible while producing the desired product in the first stage.

The present invention is based on the finding that amlodipine maleate substantially free of amlodipine aspartate byproduct can be prepared by carefully selecting reaction conditions. That is, it was found that the pH of the reaction mixture during the formation of amlodipine maleate should be substantially acidic. The process for producing amlodipine maleate substantially free of amlodipine aspartate byproduct comprises a reaction between amlodipine and maleic acid, the reaction environment being substantially acidic, which forms the basis of the present invention.

Accordingly, the first embodiment of the present invention comprises adding an amlodipine-containing starting material (referred to herein as the "amlodipine source") to a solution of maleic acid in such a way that the maleic acid in the reaction mixture is in excess relative to amlodipine, i.e., amlodipine base is added to a molar equivalent or excess of maleic acid, preferably to an excess of maleic acid. When the amlodipine raw material is added, the existing unreacted maleic acid provides an acidic pH for a reaction mixed system in the salt forming process. Preferably, the free base of amlodipine or another acid addition salt of amlodipine is added to a solution or suspension of maleic acid in a suitable solvent to form a solution, wherein the molar amount of maleic acid is at least 1.01 times, and more preferably at least 1.05 times, greater than that of amlodipine. Upon completion of the addition, amlodipine maleate precipitates as a solid. In this process, amlodipine reagent is used in the form of a solid or a solution or a suspension, which can be continuously or intermittently fed into the reaction system. Suitable minimum maleic acid excesses are about 1 mole% or more, i.e., about 1.01 times the molar amount, desirably about 5 mole% excess, and perhaps even higher, e.g., up to 50 or 100 mole%, i.e., 2 times the molar amount. The use of an excess of maleic acid facilitates the production on an industrial scale where the actual dosage of amlodipine may be difficult to determine in some cases.

The amlodipine source may be contacted with maleic acid in a solvent under pH control, where the pH is maintained below 7, preferably below 6.5, and a typical range is between 4.5 and 6.5, optionally with intermittent or continuous addition of maleic acid. At a pH below 4.5, the formation of amlodipine aspartate is also sufficiently inhibited, but other by-products are sometimes formed. Even under pH control, it is usually most convenient to add the amlodipine source to maleic acid as in the first example, but this is not strictly necessary. Upon completion of the addition, amlodipine maleate precipitates as a solid.

This process of monitoring the pH is also useful in the case where the amlodipine source is an unpurified material, since the actual content of amlodipine is often only an estimated number, and/or the amlodipine source may also contain basic impurities or by-products, which may also react with maleic acid. For example, crude amlodipine products obtained by deprotecting excess methylamine terephthalamidoamlodipine may contain trace amounts of methylamine, which can be measured, but are difficult. Thus, during the addition of the amlodipine source to the maleic acid or treatment with the maleic acid solution or suspension, the pH of the reaction mixture is monitored and adjusted, such as by the addition of acid, preferably maleic acid, to meet the requirements described above for maintaining a pH below 7.

In addition, the pH can be maintained in the acidic range by using other acid addition salts of amlodipine than maleate. The desired acidic pH is adjusted by the release of the corresponding acid from the salt molecule during maleate formation. See the reaction formula:

amlodipine, HX + maleic acid- - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - -

Wherein X represents the anion of the corresponding acid.

Since the reaction is carried out substantially in equilibrium, amlodipine salts which are more soluble than amlodipine maleate in the reaction medium should be employed. As amlodipine maleate is precipitated from the solution, the reaction equilibrium is constantly shifted towards the direction of generating more amlodipine maleate. Suitable salts are, for example: amlodipine hydrochloride, amlodipine mesylate or benzenesulfonate. In general, any suitable salt that is more soluble in the reaction solvent than amlodipine maleate may be used.

In the present invention, amlodipine from various sources can be used to react with maleic acid. For example, a mixture of the last reaction step in the synthesis of amlodipine may be used. Such schemes are known from previous art, wherein the last reaction step usually comprises a step of deprotecting the amino protecting group on the amlodipine precursor, as shown in the following reaction scheme:

in the reaction scheme, the reaction is carried out in the presence of a catalyst,represents a substituent or group which functions to protect or mask the amino group; it may include benzylamino or phthalimido groups (EP 89167), azido groups (EP 89167), tritylamino groups (EP 599220), hexamethylenetetramino groups (EP 902016) and the like. Another useful synthetic procedure for preparing high-yield, high-purity amlodipine or salts thereof is described in the public provisional patent application No. 60/258,613 (12/29/2000), the entire contents of which are incorporated herein by reference; also described in U.S. public-owned co-pending U.S. patent application 09/809,351 (3/16 2001), entitled "Process for the preparation of amlodipine, amlodipine derivatives, and amlodipine precursors," the entire contents of which are incorporated herein by reference.

After the deprotection reaction is complete, the reaction mixture can be treated in a known manner to facilitate the provision of a solution of the crude amlodipine product in a suitable solvent, such a solution being useful as a starting material for amlodipine in the process of the present invention for the preparation of amlodipine maleate free from amlodipine aspartate byproduct. Alternatively, the amlodipine free base can be isolated in solid form from the amlodipine synthesis reaction, e.g., the free base can be dosed in crude or purified form according to the procedures outlined in int.j.pharm.133, 72 (1996). Alternatively, amlodipine free base (isolated or not) may also be converted to other salts prior to contacting with maleic acid. The amlodipine source may be in solution, solid, or liquid suspension in a solvent.

As indicated previously, a key common to any process of the present invention is that the amlodipine source is contacted with maleic acid in an acidic environment. In general, the pH of the reaction mixture should not exceed 6.5 in the salt-forming reaction.

A variety of solvents or solvent systems may be suitable for use in the process of the present invention. Preferred solvents are those in which the starting reactants are sufficiently soluble and in which the product amlodipine maleate is only slightly soluble. Such solvents include water, alcohols such as methanol, ethanol, isopropanol, esters such as ethyl acetate, ketones such as acetone, nitriles such as acetonitrile, ethers such as dioxane or tetrahydrofuran, hydrocarbons such as toluene, or mixtures thereof. The advantage of the present invention is that certain solvents, such as water, which were inconvenient in the prior art processes, can be used without difficulty in the present process.

The temperature at which the amlodipine source is contacted with maleic acid may range from ambient temperature to the boiling point of the solvent or solvent system, and may also vary with the progress of the reaction. The temperature is desirably higher than 40 c because amlodipine maleate crystallizes out of the hot solution in a good and/or large particle form under such conditions. If reacted at ambient temperature, amlodipine maleate precipitates as small crystals, which tends to make the crystals difficult to filter and dry. However, the production of amlodipine aspartate is temperature dependent. It has been found that when maleic acid is added to amlodipine base in the prior art, the undesirable amlodipine aspartate is formed in large amounts at temperatures above about 40 ℃. For example, addition of maleic acid to amlodipine base in an isopropanol solvent at 80 c yields amlodipine maleate containing about 0.7% amlodipine aspartate as an impurity. However, amlodipine is added to maleic acid in response to the advantages of this patent, and higher temperatures can be used without difficulty. Especially at reaction temperatures above 40 c, e.g. if a solvent is used which requires a higher temperature for converting amlodipine or maleic acid into a solution, or if the reaction mixture needs to be concentrated by evaporation. For example, the addition of amlodipine to a 5 mole percent excess of maleic acid in a hot isopropanol solvent system can produce amlodipine maleate containing only 0.03% amlodipine aspartate as an impurity.

The importance of a substantially acidic environment, particularly the use of an excess of maleic acid to minimize the production of amlodipine aspartate, can be seen in processes for purifying amlodipine maleate from other impurities by crystallization or precipitation. Increasing the temperature in order to dissolve amlodipine maleate in the crystallization or precipitation solvent may also promote the formation of amlodipine aspartate. Since amlodipine aspartate is similar in solubility to amlodipine maleate in most crystallization solvents, conventional crystallization techniques cannot isolate amlodipine maleate therefrom, thus ironically meaning that the crystallization process "contaminates" the product. However, if an excessive amount of maleic acid is present in the crystallization system, the generation of amlodipine aspartate is minimized. The present invention further relates to a process for the precipitation or crystallization of amlodipine maleate from solution in solid form, characterized in that the amount of free maleic acid contained during the precipitation is in excess of 1 to 100 mol%, preferably in excess of 5 mol%.

The process of precipitation or crystallization of amlodipine maleate from the solution containing excess maleic acid can then be used as a purification step. Yet another aspect of the present invention relates to the production of a purified free base or salt of amlodipine by converting precipitated or crystallized amlodipine maleate. In particular, once amlodipine maleate is precipitated or crystallized from a solution containing an excess of maleic acid, it can be converted into another salt having good purity. The conversion can be achieved by directly treating amlodipine maleate in solution with a suitable acid. Alternatively, the transformation process may also comprise treating the amlodipine maleate in solution with an organic or inorganic base to form amlodipine free base, and then treating the free base, isolated or not, with the desired acid to form the desired amlodipine salt. The newly formed salt may be precipitated or otherwise removed from the solvent. Due to the good purity of the precipitated or crystallized amlodipine maleate, it can be prepared into a finished product meeting pharmaceutical quality requirements, accompanied by the conversion salt form or the free base form, without any subsequent purification at all. Examples of salts which are suitable for this process are amlodipine besylate (besylate) and amlodipine hydrochloride.

In the usual solvents suitable for the crystallization or precipitation of amlodipine maleate, such as water, methanol, ethanol, isopropanol, acetone, acetonitrile, ethyl acetate, toluene and mixtures thereof, the necessary excess of maleic acid should advantageously be from at least 1 mol% up to 100 mol%, preferably between 5% and 25%. The appropriate amount of maleic acid in an industrial process can be determined by a set of ordinary experiments according to the respective conditions, considering factors such as the type of solvent, concentration and temperature range, and taking yield and purity as evaluation indexes.

Amlodipine maleate "substantially free" of amlodipine aspartate byproduct means that amlodipine maleate contains less than 1 wt% of amlodipine aspartate, more preferably less than 0.5 wt%, and still more preferably less than 0.2 wt%, most preferably less than 0.1 wt%. Amlodipine maleate substantially free of amlodipine aspartate may be used for therapeutic purposes as a pharmaceutically acceptable amlodipine salt. Accordingly, amlodipine maleate substantially free of amlodipine aspartate forms another component of the present invention.

Amlodipine molecule has a chiral center on the tetrahydropyridine ring, so that two optically active forms exist. The two forms can be selected as salts, for example, a salt formed by an optically active base or acid, and can be separated by crystallization or chromatography, and then can be converted into the amlodipine maleate single isomer according to the present invention by the above process. Individual isomers or isomer mixtures of amlodipine maleate are employed in the present invention. Accordingly, individual isomers or isomer mixtures of amlodipine maleate substantially free of amlodipine aspartate are also within the scope of the present invention.

Amlodipine maleate substantially free of amlodipine aspartate can be used as a calcium channel blocker and thus can be used for any heart disease that can benefit from treatment with a calcium channel blocker. In particular, amlodipine maleate without amlodipine aspartate can be used to treat or prevent hypertension or angina by allowing a patient in need thereof to take an effective amount. The type of angina pectoris is not particularly limited herein, and mainly includes chronic stable angina pectoris and vasospastic angina pectoris (Prinzmetal's angina). The compounds may be administered by any suitable route, including orally and parenterally. A "patient" to be treated includes humans and animals, particularly humans and mammals.

The compounds are typically administered as part of a pharmaceutical composition. Accordingly, a further aspect of the present invention is directed to a pharmaceutical composition for treating or preventing hypertension or angina which consists of an effective amount of amlodipine maleate substantially free of amlodipine aspartate and pharmaceutically acceptable excipients. Excipients include any inert or inactive material useful in the preparation of pharmaceutical dosage forms. For example, tablet excipients include, but are not limited to, calcium phosphate, cellulose, starch, or lactose. Those capsules made of gelatin may contain or be loaded with amlodipine maleate alone or in admixture with other excipients. Liquid dosage forms such as oral liquids in the form of solutions or suspensions, and injections are also included. The pharmaceutical composition can be formulated for transdermal administration in the form of a patch. All of the above pharmaceutical compositions may optionally be formulated with one or more of the following excipients: carrier, diluent, colorant, essence, lubricant, solubilizer, disintegrating agent, adhesive and preservative.

The pharmaceutical compositions are often administered in unit doses. Unit doses are typically administered once or twice a day, more typically once a day. In the case of transdermal patches, the unit dose (a single patch) is administered at least once a month, more commonly once every two weeks, most typically once a week. The effective amount of amlodipine maleate without amlodipine aspartate in a unit dose for the treatment or prevention of hypertension or angina is generally in the range of 1-100mg, typically 1-50mg, more typically 1-20 mg. In solid oral dosage forms (tablets, capsules, etc.), the typical amlodipine maleate content of the pharmaceutical composition is about 1, 2.5, 5.0 or 10mg, respectively. For simplicity, all levels refer to the corresponding amount of amlodipine free base added to the composition. For hypertensive angina a typical human initial oral dose is 5mg once daily, up to 10mg once daily. The starting dose for young, infirm or elderly individuals, or patients with liver function deficits may be 2.5mg once daily, which may also be used when amlodipine is used in combination with other antihypertensive therapies. Specific examples of such pharmaceutical compositions include those described in EP 244944, in which amlodipine maleate is used as the active ingredient according to the present invention.

The preferred pH of the pharmaceutical composition is in the range of about 5.5 to 7.0 when measured in a 20 wt% aqueous slurry as described more fully in U.S. public provisional patent application (common-owned co-pending US patent application 09/809,346 (16/3 2001) entitled "pharmaceutical composition containing amlodipine maleate", the entire contents of which are incorporated herein by reference. These compositions have good or improved stability overall.

All of the above pharmaceutical compositions can be prepared by known methods or techniques. For example, tablets may be prepared by dry granulation/direct compression or by classical wet granulation methods. Representative tablet formulations are prepared by mixing, filling and compressing the ingredients into tablets. The mixing step may comprise wet granulation or dry granulation. Similarly, capsules may be prepared by mixing the components and filling into capsules.

The above composition can also be used for relieving heart failure symptoms, improving left ventricular systolic function, improving exercise endurance of ischemic left ventricular dysfunction patients, and treating heart failure without angina pectoris.

The amlodipine maleate composition of the present invention may also be used in combination therapy with other antihypertensive and/or antianginal drugs, for example with ACE (angiotensin converting enzyme) inhibitors such as benazepril. The combination can be achieved in a single mixed formulation (e.g., a capsule containing both amlodipine maleate and benazepril hydrochloride) or in a form in which the above-mentioned drugs are administered separately. Similarly, amlodipine maleate can also be used in combination with HMG-CoA reductase inhibitors, particularly statins such as lovastatin, simvastatin, atorvastatin, and the like.

Accordingly, the present invention further provides a method for treating and/or preventing any one or more symptoms of angina pectoris, hypertension, heart failure by administering the pharmaceutical composition of the present invention containing an effective and/or preventive dose of amlodipine maleate to a patient in need thereof.

When preparing amlodipine maleate as an active ingredient or as a component in a pharmaceutical composition, it is analyzed whether and/or how much amlodipine aspartate is contained should be beneficial to ensure that the active ingredient or component is free of amlodipine aspartate impurities. This is useful, for example, in examining the effectiveness of the crystallization conditions selected when preparing amlodipine maleate substantially free of amlodipine aspartate according to the present invention. Methods for assaying amlodipine aspartate and how to prepare amlodipine aspartate control standards or control markers are more fully described in U.S. public-owned co-pending US patent application 09/809,347 (3/16 2001), entitled "control standards for determining amlodipine maleate purity or stability and preparation thereof," the entire contents of which are incorporated herein by reference.

Examples

Example 1 preparation of amlodipine maleate from amlodipine crude

Step 1 isolation of Benzodicamidoamlodipine

Into the reactor A1 were charged 64 liters of a 40% aqueous methylamine solution and 8.0 kg of phthalimidamlodipine with stirring. The suspension was stirred at 40-45 ℃ for 8 hours. 120 l of toluene were then added and the mixture was stirred for 30 minutes. The mixture was then allowed to stand for separation and the aqueous layer was separated and discarded. The toluene layer was washed with 40 liters of water. The toluene solution was concentrated at 60 ℃ on a rotary evaporator until the initial precipitation (volume about 12 l) had occurred. The residue was poured into a vessel, the evaporator was washed with 4 liters of ethanol, and the washings were combined with the toluene solution. The amount of amlodipine in the solution is determined by titration. As a result: 6.13 kg.

Step 2 formation of amlodipine maleate

1.83 kg of maleic acid are dissolved in 70 l of ethanol at 50-55 ℃ in a reactor A2. The solution was filtered into a clean reactor a1 by pressure filtration. Reactor a2 and the filter were washed with 7 liters of ethanol. The combined solution was warmed to 50-55 ℃.

6.13 kg of amlodipine free base from the previous step was charged into reactor A2 and 66 liters of ethanol were added. The solution was fed from reactor A2 to the stirred solution in reactor A1 by pressure filtration (pressurized with nitrogen). The reactor and filter were washed with 7 liters of ethanol. The temperature in reactor a1 was naturally raised to 65 ℃ (no cooling required). The mixture was then stirred and allowed to cool slowly to 15-20 ℃. The precipitated solid product is filtered off on an upper and lower vacuum filter (nutche filter), the product on the filter is washed with 2X 4 l of ethanol and dried at about 40 ℃.

Yield: 5.85 kg of amlodipine maleate.

Purity (HPLC): the content of amlodipine aspartic acid is less than 0.05 percent

Particle size: average 80-100 microns

In contrast thereto

5 kg of wet amlodipine free base was suspended in 17.5 l of isopropanol. The suspension was heated to 65 ℃ to obtain a clear solution. 1.17 kg of maleic acid was added in portions. The temperature was raised to 70 ℃ to give a clear solution again. Crystallization was initiated by adding seeds and raising the temperature to 72.5 ℃. The mixture was cooled to 30 ℃ over 1.5 hours and further cooled to 2 ℃ over 1 hour. The crystals were filtered off and washed with 3X 5.8 l of isopropanol and dried in a vacuum oven at 40 ℃ for 2 days.

Yield: 4960 g

Purity: the content of amlodipine and aspartic acid is 0.63 percent

Example 2

0.58 g of maleic acid was dissolved in 25 ml of water and heated to about 60 ℃. To this solution was added 2.0 g of amlodipine in portions. The solution turned pale yellow during the addition and a solid began to precipitate from the mixture after the addition was complete. The mixture was slowly cooled to room temperature and the solid was filtered off. The solid was washed with 5 ml of water and dried in a vacuum oven at 50 ℃ for 24 hours, leaving 2.4 g (93%) of the product as a white solid.

HPLC: the content of amlodipine and aspartic acid is 0.01 percent

NMR (nuclear magnetic resonance): in compliance with amlodipine maleate

In contrast thereto

2.0 g of amlodipine is suspended in 25 ml of water and heated to about 60 ℃. To this suspension 0.58 g of maleic acid was added in portions. The suspension became clear (slightly yellow) and the solid began to precipitate out. The mixture was slowly cooled to room temperature and the solid was filtered off. The solid was washed with 5 ml of water and dried in a vacuum oven at 50 ℃ for 24 hours, leaving 2.4 g (93%) of the product as a white solid.

HPLC: the content of amlodipine and aspartic acid is 0.2 percent

NMR: amlodipine maleate + about 10% amlodipine free base

Example 3

Preparation of amlodipine maleate from amlodipine hydrochloride

1 g of amlodipine hydrochloride was dissolved in 20 ml of water. To this solution 0.26 g maleic acid was added and the mixture was stirred until all dissolved. After a few minutes a solid precipitated out and the mixture was stirred at room temperature for 1 hour. The solid was filtered off on filter paper and washed with 2 x 5 ml of water. After drying in a vacuum oven 0.72 g (61%) of solid product was obtained.

Amlodipine aspartate content (HPLC): 0.01 percent

Example 4

Preparation of amlodipine maleate from amlodipine mesylate

1 g amlodipine hydrochloride mesylate was dissolved in 42 ml water. To this solution 0.23 g maleic acid was added and the mixture was stirred until a clear solution was obtained. After a few minutes a solid appeared and the mixture was stirred at room temperature for 1 hour. The solid was filtered off on filter paper and washed with 2 x 5 ml of water. After drying in a vacuum oven 0.73 g (70%) of the product was obtained as an off-white solid.

Amlodipine aspartate content (HPLC): 0.01 percent

Example 5

Crystal of amlodipine maleate

5 g amlodipine maleate was dissolved in a refluxing mixture of 60 ml ethanol and 0.055 g maleic acid. The solution is cooled in a refrigerator to 5-10 ℃ and the precipitate is filtered off and dried.

Yield: 4.5 g

HPLC (IN): the content of amlodipine aspartic acid is 0.046%

In contrast thereto

20 g amlodipine maleate was dissolved in 240 ml ethanol reflux. The solution was cooled to 20 ℃ and the precipitate formed was filtered off and dried.

Yield: 16.3 g

HPLC (IN): the content of amlodipine aspartic acid is 0.67 percent

Reference examples

Preparation of amlodipine aspartate as a control Standard

16 g of amlodipine and 12 g of amlodipine maleate were thawed in a 300ml flask. The melt is cooled to the chamberThe mixture was warmed and dissolved in 300mL of dichloromethane. The mixture was extracted with 300ml of 1M NaOH solution. The organic layer was discarded and the aqueous layer was neutralized with 55 ml of 6M HCl solution. The mixture was extracted with 300ml of dichloromethane. The organic layer was separated with Na₂SO₄And (5) drying. The mixture was evaporated to dryness and the resulting waxy solid was recrystallized from ethanol. The sticky solid was dried in a vacuum oven at 40 ℃ leaving 4.7 g of off-white product.

Yield: 4.7 g (39%)

Melting point: 178 ℃ -183 ℃ (decomposition)

It will be apparent to those skilled in the art from this disclosure that various changes and modifications can be made, or equivalents employed, in the practice of the concepts and embodiments thereof without departing from the spirit and scope of the invention as defined in the following claims.

Claims (15)

1. A process comprising reacting amlodipine or an acid addition salt thereof with maleic acid in an acidic environment to form an amlodipine maleate product, wherein the relative molar amount of maleic acid to amlodipine being added is at least 1.05: 1.

2. The process of claim 1, wherein said amlodipine maleate product contains less than 1 wt% amlodipine aspartate, based on the amount of amlodipine maleate.

3. The process according to claim 2, wherein said amlodipine maleate product contains less than 0.2 wt% amlodipine aspartate, based on the amount of amlodipine maleate.

4. The process of claim 1, wherein said amlodipine maleate comprises less than 1% by weight of amlodipine aspartate, wherein said amlodipine is added to the maleic acid solution or suspension in a continuous or batch manner to form a solution; and amlodipine maleate in solid form is isolated from the solution.

5. The process of claim 4, wherein the amlodipine source is selected from the group consisting of crude amlodipine obtained after the amlodipine synthesis reaction, purified amlodipine free base and acid addition salts of amlodipine other than maleate.

6. The process of claim 5, wherein said source of amlodipine is in a solid state or dissolved in a solvent.

7. The process of claim 1, wherein amlodipine maleate comprises less than 1% by weight of amlodipine aspartate, wherein amlodipine is contacted with a solution or suspension of maleic acid under pH control in a continuous or batch manner to form a solution, wherein the pH of the solution does not exceed 6.5; the amlodipine maleate is isolated from the solution as a solid.

8. The process of claim 7, wherein the amlodipine source is selected from the group consisting of crude amlodipine obtained after the amlodipine synthesis reaction, purified amlodipine free base and acid addition salts of amlodipine other than maleate.

9. The process according to any one of claims 7 or 8, wherein said source of amlodipine is in a solid state or dissolved in a solvent.

10. The process according to claim 1, wherein said source of amlodipine is an acid addition salt of amlodipine other than the maleate salt, in solid form or dissolved or suspended in a suitable solvent.

11. The process of claim 1, wherein said amlodipine source is added to said maleic acid solution or suspension.

12. The process of claim 1, further comprising crystallizing or precipitating amlodipine maleate from a solution thereof, wherein said solution contains an excess of maleic acid.

13. The process according to claim 12, further comprising converting said amlodipine maleate to another acid addition salt.

14. The process according to claim 12, wherein said amlodipine maleate is converted to amlodipine besylate, amlodipine hydrochloride or amlodipine mesylate.

15. The process of claim 14, wherein said converting comprises treating said amlodipine maleate with a base to produce amlodipine free base and treating said amlodipine free base with benzenesulfonic acid, methanesulfonic acid or hydrochloric acid.