The present application pertains to the field of pharmaceutical research and development, in particular to a method for preparing a suspension of vortioxetine pamoate, and to a method for preparing a lyophilized vortioxetine pamoate powder for injection.
Vortioxetine (chemically named as 1-[2-(2,4-dimethylphenylsulfanyl)phenyl]piperazine) is an antidepressant jointly developed by Takeda Pharmaceuticals and Lundbeck Pharmaceuticals, the structural formula of which is as follows:
Vortioxetine can effectively overcome some shortcomings of common antidepressants, such as weight gain, drowsiness, medicament sedation, and other adverse reactions, and has the advantages of multiple targets, low adverse reaction rate, low relapse rate, safety and tolerance for continuous treatment, and the like. Currently, the marketed ones are vortioxetine hydrobromide tablets, which have a shorter duration of efficacy in the body and need to be taken once a day.
It is disclosed in WO2017167180A1 that, for the first time, vortioxetine and pamoic acid were made into a salt in a certain ratio, which prolonged the residence time of vortioxetine in vivo and thus achieved a slow release of vortioxetine in vivo. Vortioxetine pamoate was prepared into a stable long-acting preparation, allowing the administration to the patient once every two or four weeks, thereby greatly improving the utilization efficiency of the medicament, improving the therapeutic efficacy of the medicament, improving the patient's compliance and reducing adverse reactions.
It is mentioned in WO2017167180A1 that the vortioxetine pamoate was administered as a suspension, wherein the pharmaceutically acceptable carrier is preferably a viscous injectable carrier, for example, a viscous injectable carrier having a viscosity of at least 20 cp at 20° C. High viscosity results in bigger difficulty in preparing the suspension before clinical use, higher force to withdraw the suspension into the syringe after preparation, and higher requirements for operators. In addition, if vortex is needed in preparation (such as a vortex for 2 min), it is required to use an external equipment such as a vortex machine, which increases the difficulty and time of preparation. For the preparation of a suspension, even if a uniformly mixed suspension can be obtained eventually, the operation process may be complex, time-consuming and laborious, and there is still a risk that the API may form into small aggregates that are difficult to be dispersed.
An object of the present application is to provide a vortioxetine pamoate powder for injection and a preparation method therefor, which is realized by the following technical embodiments.
Firstly, the present application provides a powder for injection consisting of vortioxetine pamoate and pharmaceutically acceptable excipients.
In some embodiments of the present application, the mass percentage of the vortioxetine pamoate is 54.0% to 72.4%, based on total mass of the composition.
In some embodiments of the present application, the pharmaceutically acceptable excipients comprise a suspending agent selected from the group consisting of a low molecular weight suspending agent and a high molecular weight suspending agent, including glycerol, arabic gum, agar, tragacanth gum, methyl cellulose, sodium carboxymethyl cellulose, hydroxypropyl cellulose, povidone, glucan, carbopol, aluminum monostearate, and the like. The suspension agent accounts for 2.3% to 13.8% (w/w), preferably 6.9% to 10.8% (w/w) of the total mass of the powder for injection. The suspending agent is preferably sodium carboxymethyl cellulose, more preferably sodium carboxymethyl cellulose having a viscosity of 50 cp to 200 cp (4%, w/v).
In some embodiments of the present application, the pharmaceutically acceptable excipients further comprise a freeze-drying protective agent selected from the group consisting of saccharides and polyols, such as sucrose, trehalose, lactose, xylitol, glucose or mannitol. Preferably, the freeze-drying protective agent accounts for 4.6% to 35.0% (w/w) of the total mass of the powder for injection.
In some embodiments of the present application, the pharmaceutically acceptable excipients further comprise an osmotic pressure adjuster selected from the group consisting of sodium chloride, potassium chloride, mannitol, glucose, borax, and the like.
In some embodiments of the present application, the mannitol is preferred as the osmotic pressure adjuster and the freeze-drying protective agent, and the injection grade mannitol is further preferred. Mannitol accounts for 20.7% to 32.5% (w/w) of the total mass of the powder for injection.
In some embodiments of the present application, the pharmaceutically acceptable excipients are preferably free of a wetting agent, such as polysorbate (also known as Tween) and poloxamer. Wetting agent, playing a dispersing function in a formulation, can improve the mixing uniformity of a suspension. However, the inventors unexpectedly found that the prepared suspension will settle rapidly if a wetting agent such as polysorbate is added to the formulation of the present application.
The preferred formulation of the present application consists of vortioxetine pamoate monohydrate, sodium carboxymethyl cellulose, mannitol and water for injection.
The preferred preparation specification of the present application is 140 mg to 280 mg, which is equivalent to about 235.5 mg to 471.0 mg of vortioxetine pamoate monohydrate, wherein, preferably, the amount of sodium carboxymethyl cellulose is 6.9% to 10.8% (w/w), and the amount of mannitol is 20.7% to 32.5% (w/w).
The components and amounts of the preferred vortioxetine pamoate powder for injection of the present application are as follows:
In some embodiments of the present application, the vortioxetine pamoate has a particle size of 1 μm to 40 μm (D90), preferably 1 μm to 20 μm (D90), more preferably 1 μm to 10 μm (D90).
D90 refers to the corresponding particle size when the cumulative particle size distribution of the sample measured by a laser granulometer reaches 90%.
The present application further provides a preparation method of vortioxetine pamoate powder for injection, comprising the following steps:
The particle size in step (3) is preferably 1 μm to 20 μm (D90), more preferably 1 μm to 10 μm (D90).
Particle size has a great influence on the properties, syringeability and bioavailability of the product. A wide particle size distribution or a poor mixing uniformity will lead to caking and sedimentation, resulting in needle blockage. In the preparation process of the present application, a high-shear mixing machine and a high-pressure homogenizer are used to adjust the particle size to the desired range.
This step provides a method of preparing a lyophilized formulation of vortioxetine pamoate, comprising the following steps:
The inventive concepts of the present application are as follows.
The powder for injection prepared according to the present application has uniformly dispersed particles and normal appearance, and the internal structure of solid matter in the broken vial is uniform without shrinkage. After adding water for injection, the powder for injection can be quickly reconstructed (a uniformly mixed suspension can be obtained after a gentle shake for less than 30 s), and the reconstructed solution can pass through a needle with a size of 19 G to 22 G, indicating a good permeability. The development of this preparation not only improves the feasibility of industrialization, but also reduces the difficulties in medicament transportation and storage, thereby providing a more effective and convenient treatment for clinical mental patients.
In order to explain the Examples of the present application and the technical solutions of the prior art more clearly, the following briefly introduces the drawings used in the Examples and the prior art. Obviously, the drawings in the following description are only some Examples of the present application, and for those skilled in the art, other drawings may be obtained based on these drawings.
The ordinate TSI is the stability index, which is an evaluation of the stability of the whole dispersion system, and the stability decreases with the increase of the value of TSI.
The present application will be further described in detail below in conjunction with Examples, so that those skilled in the art can understand and practice the present application more clearly. However, the present application is not limited to the following Examples, and any changes, modifications and equivalent substitutions made to the present application without departing from the spirit and scope of the present application are within the scope of the present application.
The product obtained in Example 1 (with polysorbate 80, referred to as TW80) and the product obtained in Example 2 (without TW80) were analyzed by a stability analyzer (model: TURBISCAN Lab) for the relationship between time and sedimentation, and the results are shown in
The experimental results showed that for the system without polysorbate 80, the sedimentation rate of the active pharmaceutical ingredient particles was low. For the system introduced with polysorbate 80, the sedimentation rate of the active pharmaceutical ingredient particles was high and the layering phenomenon was obvious. The results showed that the properties of the suspensions of the two different systems were quite different, and the medicament solution without polysorbate 80 was better than that with polysorbate 80.
With reference to Example 2, samples with different particle sizes were obtained by changing the working pressure of the high-pressure homogenizer in step (3). The relationship between time and sedimentation was analyzed by stability analyzer, and the result was shown in
In
The experimental results showed that for the obtained active pharmaceutical ingredient particles, the particle size and the sedimentation rate were decreased, and the stability was improved, when the working pressure of the high-pressure homogenizer was increased.
The particle size distribution was measured by a laser granulometer, such as by light scattering or laser diffraction techniques. In order to determine the particle size, for example, the powder was loaded into a laser diffraction spectrometer through a dispersion unit. The test method is described in detail as follows:
The instrument was set up according to the above parameters. A sample was taken and reconstructed with 1 mL to 3 mL of water to prepare a suspension. The purified water was then added to dilute 10 to 50 times the original volume of the solution. An appropriate amount of the treated sample was added to the injection cell. The addition of the sample should be performed under even and continuous stirring. After the cycle was stable for 1 min, the cycle was performed 3 times for measurement and the average value was taken.
The above description is only the preferred Examples of the present application, and is not intended to limit the present application. Any modifications, equivalent substitutions, improvements, and the like made within the spirit and principles of the present application should be included within the scope of the present application.
Filing Document | Filing Date | Country | Kind |
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PCT/CN2021/110851 | 8/5/2021 | WO |