The present invention relates to the crystalline form of phentermine hydrochloride monohydrate and the process for obtaining said crystalline form. The present invention is in the fields of chemistry and pharmacy.
Phentermine or 2-methyl-1-phenylpropan-2-amine is commonly found in the hydrochloride salt form (#CAS 1197-21-3) and it is a central nervous system stimulant used as an appetite suppressant and stimulant in medicaments. Such a compound and its synthetic route are described in the U.S. Pat. No. 2,408,345, whose priority date is Apr. 13, 1942. It has the molecular form C10H16CIN and the following structure:
Polymorphic forms of a given substance may have different chemical and physical properties, such as melting point, chemical reactivity, solubility, dissolution rate, rheological properties and density. These properties can directly affect the processability and manufacture of the active and the pharmaceutical form containing said active, as well as stability, dissolution and bioavailability. In this way, polymorphism can impact the quality, safety and efficacy of a pharmaceutical product.
The term polymorphism, used in the field of pharmaceutical and chemical sciences, is defined as the ability of chemical compounds to exist in two or more crystalline structures. When the solvent is incorporated into the compound's crystalline network in stoichiometric or non-stoichiometric amounts, molecular adducts called solvates, also called pseudopolymorphs, are formed. Solvates with incorporated water molecules, on the other hand, are called hydrates. According to the number of incorporated molecules , the hydrate has a different name, such as: monohydrate—1 molecule of water; sesquihydrate—1.5 molecules of water, dihydrate—2 molecules of water, and so on.
Several methodologies can be used to characterize an active pharmaceutical ingredient polymorphs'. Demonstration of a distinct structure by single crystal X-ray diffraction is considered definitive evidence for polymorphism. However, polycrystal X-ray diffraction in conjunction with other techniques including microscopy, thermal analysis (e.g., differential scanning calorimetry, thermogravimetric analysis, and hot stage microscopy), and spectroscopy (e.g., infrared absorption, Raman scattering, and nuclear magnetic resonance) can also be used for crystalline forms' characterization.
An anhydrous crystal form of phentermine hydrochloride, characterized by the X-ray diffraction shown in
U.S. Pat. Application 2008/293695 describes many phentermine salts and their polymorphs, such as phentermine pamoate, phentermine xinafoate, phentermine salicylate. Additionally, U.S. Pat. No. 8,334,322 specifically describes phentermine pamoate polymorph. Nonetheless, none of these documents disclose polymorphs or pseudopolymorphs of phentermine hydrochloride.
Phentermine hydrochloride in anhydrous form has a gain of about 7.5% by mass at 80% relative humidity, being classified as hygroscopic according to the British Pharmacopoeia, 2016 edition (British Pharmacopoeia). This fact can cause dosage problems if the active is manipulated under high humidity conditions. These handling and hygroscopicity problems bring to light the need for new solid forms of phentermine hydrochloride that provides better processing properties, such as ease of handling, storage stability and ease of purification.
Crystal forms' diversity of a given active increases the portfolio of materials available to the formulation scientist optimize pharmaceutical formulations, since there are differences among crystal forms. As an example, one can cite polymorph's different crystalline habits, greater crystallinity, less susceptibility to humidity and stability, technical features responsible for improving the manufacturing process and manipulation, dissolution profile and shelf-life.
The present disclosure provides a crystalline form of phentermine hydrochloride monohydrate and processes for obtaining the same. The said crystalline form promotes advantages to phentermine hydrochloride due to its stability and lower hygroscopicity when compared to the anhydrous form of the same salt, the monohydrated form can also be produced in different crystalline habits (prismatic or placoid) depending on the method of production used, promoting better processing properties such as ease of handling and storage stability. Furthermore, the active's bioavailability in several pharmaceutical compositions, such as tablets, gelatin capsules, powders, granules, solutions or suspensions, can also be improved.
The present invention provides the following objects as inventive concepts.
A first object of the invention is the crystalline form of phentermine hydrochloride in the monohydrated form. A second object of the invention are processes for obtaining the crystalline form of phentermine hydrochloride as described in the first object and in its embodiments.
The present invention consists of the definition of a new crystalline form of phentermine hydrochloride monohydrate, obtained in an unexpected and surprising way, since phentermine's molecule was first described in 1942 and no further crystalline forms of its hydrochloride salt have been described in the state of the art. Additionally, processes for obtaining said crystalline form are described, preferably high shear granulation and drying in a fluidized bed.
The crystalline form of phentermine hydrochloride monohydrate is obtained from the anhydrous salt form by recrystallization of suspension or solution thereof in pure water or solvent mixture containing water, or by wet granulation process using high shear. The remaining crystalline material is dried in an oven or fluidized bed to remove solvent or residual water. Alternatively, it is possible to use a mixture of water with more volatile solvents in the obtaining process to reduce the time of the drying process.
Another way of obtaining the crystalline form of the present invention is exposing the anhydrous form to an environment with a high humidity content (above 90% RH) using a chamber with controlled humidity.
Further widely used methods in the pharmaceutical industry, such as lyophilization, drying via spray drying and drying in a vacuum oven, are viable alternatives for preparing the crystalline form of the present invention.
In the present invention, the term “monohydrate” refers to the hydrate in which a water molecule is incorporated into the crystalline structure, associated with a phentermine hydrochloride molecule, wherein the stoichiometry is 1:1.
In the present invention, the expression “peaks expressed in degrees 2-theta” refers to the characteristic peaks of the X-ray diffractogram obtained using a wavelength of 1.54 Å (Cu K-alpha) of the phentermine hydrochloride monohydrate form.
In a first object, the crystalline form of phentermine hydrochloride is the monohydrate form. In one embodiment, the crystalline form comprises peaks expressed in degrees 2-theta (±0.2°) at 13.3; 13.7; 14.3; 14.7; 15.1; 16.0; 18.4; 19.5; 20.5; 21.2; 22.2. 22.7; 23.3; 24.4; 24.8; 25.8; 26.4; 27.4; 28.2; 28.6; 29.1; 29.8; 30.5; 31.6; 32.3; 32.9; 34.2; 34.9; 36.0; 36.6; 37.3; 38.2; 39.5; 40.0; 40.4; 43.1; 43.6; 45.1; 46.1; 47.1; 47.6; 48.9; 52.9 and 54.2 on its X-ray diffractogram. In one embodiment, the crystalline form comprises specific peaks expressed in degrees 2-theta (±0.2°) at 13.7; 14.7; 15.1; 16.0; 18.4; 22.2; 24.8; 26.4; 28.6 and 29.8.
In one embodiment, the crystalline form comprises the bands 849, 918, 1030, 1074, 1082, 1151, 1173, 1181, 1134, 1380, 1396, 1449, 1454, 1468, 1528, 1533, 1618, 1632, 1650, 2804, 2894, 2935, 2973, 2987, 3066, 3144, 3148 and 3415 cm−1 in their absorption spectrum in the infrared region wherein the band at 3415 cm−1 refers to the water molecule.
In a second object, the process of obtaining the crystalline form of phentermine hydrochloride defined in the first object and in its embodiments comprises the steps of: (a) High shear granulation of phentermine hydrochloride in anhydrous form; (b) Addition of granulating solution in the mixture of the granulate form (a); (c) Mixture of the granulate of (a) and the granulating solution of (b) to obtain a powder; and, (d) Drying of the powder in a fluidized bed or in an oven or in a vacuum oven.
In one embodiment, said granulating solution of step (b) is water added at a rate equal to or above 5 mL/min and step (c) takes place at a mixing speed of at least 100 rpm. In a preferred embodiment, the mixing speed ranges from 100 to 150 rpm, more specifically 150 rpm. In another embodiment, the water addition rate ranges from 5 to 30 mL/min. In one embodiment, in step (d), the drying of the powder is in a fluidized bed with a maximum inlet air temperature of 60° C. and the drying of the material occurs until the obtention of a pure monohydrated form. In a preferred embodiment, drying occurs between 5 and 15 min. In a preferred embodiment, the process parameters can be jointly optimized to obtain the pure monohydrate form.
Alternatively, the process for obtaining the crystalline form of phentermine hydrochloride comprises the steps of: (a) Recrystallization of the anhydrous form suspension or solution of the phentermine hydrochloride in water or in a mixture of water and volatile solvents; and (b) Drying in an oven or vacuum oven or vacuum filtration of the solution.
In one embodiment, the said recrystallization of the solution occurs at low temperature or with heating and the said recrystallization of the suspension is maintained under magnetic stirring, at a temperature of 25° C. for 24 h. In another embodiment, said low temperature recrystallization takes place between 2 and 8° C. In another embodiment, said recrystallization is performed with heating above 60° C.
In one embodiment, said volatile solvents of step (a) are selected, without limitation, from the group consisting of methanol, ethanol, propanol, isopropanol, acetone, dichloromethane or a mixture thereof.
Alternatively, the obtaining process may comprise the steps of: (a) Exposure of the anhydrous form of phentermine hydrochloride to an atmosphere with high humidity conditions in a controlled humidity chamber; and (b) Drying in an oven or vacuum oven.
In one embodiment, said high humidity condition ranges from 90 to 95% RH. In a preferred embodiment, said humidity condition is 95% RH.
The crystalline form of phentermine hydrochloride monohydrate was characterized and differentiated from the anhydrous form using X-ray diffraction techniques, infrared absorption spectrometry, Raman spectroscopy, thermal analysis (thermogravimetry and differential scanning calorimetry), accelerated stability study, optical microscopy and hot stage optical microscopy and dynamic water vapor sorption experiments.
Table 1 contains the angles and relative intensity of the main peaks in the X-ray diffractogram (
The absorption spectrum in the infrared region of the phentermine hydrochloride monohydrate form is shown in
The Raman spectrum of the crystalline form of phentermine hydrochloride in the monohydrate form is shown in
The analysis of the crystalline habit was carried out by optical microscopy, aiming to define the crystalline habit of the monohydrated form and compare it with that of the anhydrous form. In this analysis, it was proved that different habits could be obtained for the monohydrated form depending on the process of obtaining it.
The thermal analysis performed through thermogravimetry (Thermogravimetric Analysis, TGA) (
The Differential Scanning calorimetry (DSC) experiment (
The DSC curve showed that, in the heating process, the monohydrate form converts to the anhydrous form above 50° C., as indicated by the endothermic event in the DSC curve and by X-ray diffraction measurements performed with the sample of the monohydrate form submitted to heating at 60° C. with subsequent cooling to room temperature (
Such conversion from the monohydrate form to anhydrous form can also be monitored via hot stage optical microscopy, as shown in
Therefore, from the DSC experiments and hot stage microscopy results, the conversion from the monohydrate form to the anhydrous form can be observed.
The following examples serve to illustrate aspects of the present invention without having, however, any limiting character.
100 g of phentermine hydrochloride in anhydrous form was granulated using a high shear granulation process. Initially, the homogenization of the raw material was carried out for 3 minutes, under conditions of mixing speed of 150 rpm and chopper speed of 1500 rpm, maintained throughout the process. Next, the granulating solution (20 mL of deionized water) was added for a period of 4 minutes (5 mL/min). The granulated active powder was transferred to a fluidized bed, where it remained for 10 min, with an inlet air temperature of 35° C. and an inlet air flow of 20%, having time to clear the filters with beat every 15 seconds, keeping the powder temperature close to 25° C. The drying time must be adjusted according to the granulate final humidity, which guarantees the obtention of the pure monohydrated form. The best drying time was defined by sample aliquots taken throughout the process. Times of 5, 10 and 15 minutes were checked and it was found that 10 minutes is the preferred time for such conditions. The granulate can be sampled and moisture checked using a moisture analyzer or a drying oven. The final product was characterized by infrared absorption spectroscopy and X-ray diffraction consistently indicating the formation of the phentermine hydrochloride monohydrate form with a placoid habit.
The process parameters can be jointly optimized to obtain the pure monohydrate form.
25 g of phentermine hydrochloride in anhydrous form were added to 50 mL of deionized water at a temperature of 25° C. The obtained suspension was maintained under magnetic stirring at room conditions (25° C.) for 24 hours. Microscopic analysis indicated a change in crystalline habit to a placoid shape. The suspension was vacuum filtered and the recovered crystals were characterized by infrared absorption spectroscopy and X-ray diffraction consistently indicating the formation of the phentermine hydrochloride monohydrate form with a placoid habit.
25 g of phentermine hydrochloride in anhydrous form was dissolved in 100 mL of deionized water at a temperature of 25° C. The solution was maintained cooled in an ice bath at a temperature of 2 to 8° C. for a period of 24 hours. The formation of long prismatic crystals was observed at the bottom of the solution container. The solution was vacuum filtered and the recovered crystals were characterized by infrared absorption spectroscopy and X-ray diffraction consistently indicating the formation of the phentermine hydrochloride monohydrate form with prismatic habit.
25 g of phentermine hydrochloride in anhydrous form was dissolved in 100 mL of deionized water at a temperature of 25° C. The solution was maintained on a heating plate at a temperature of 60° C. for a period of 24 hours. Crystal formation was observed at the bottom of the solution container after a few hours. The solution was then vacuum filtered and the recovered crystals were characterized by infrared absorption spectroscopy and X-ray diffraction consistently indicating the formation of the phentermine hydrochloride monohydrate form with prismatic habit.
Example 5—Process for Obtaining of the Monohydrated Crystalline Form of Phentermine Hydrochloride in a Chamber with Controlled Relative Humidity
100 mg of phentermine hydrochloride in anhydrous form was maintained in a chamber with a controlled relative humidity of 95% and a temperature of 25° C. for a period of 24 hours. The final product was characterized by infrared absorption spectroscopy and X-ray diffraction consistently indicating the formation of the phentermine hydrochloride monohydrate form with a prismatic habit.
Phentermine hydrochloride monohydrate's stability was tested by keeping 25 g of sample in an oven under conditions of 50° C. and 75% relative humidity for 30 days, as recommended by the FDA guide (Food and Drug Administration, Guidance for Industry Q1A(R2) Stability Testing of New Drug Substances and Products, November 2003 rev.2). After the accelerated stability test was carried out, it was observed by absorption spectroscopy in the infrared region (
It should be understood that the embodiments described above are merely illustrative and that any modifications thereto may occur to a person skilled in the art. Consequently, the present invention should not be considered limited to the embodiments described herein.
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/BR2020/050290 | 7/27/2020 | WO |