Disclosure of Invention
Problems to be solved by the invention
In order to solve the problems, the invention provides a pharmaceutical composition containing phenylpyrimidinone hydrochloride, a pharmaceutical preparation containing the same, and a preparation method and application of the pharmaceutical composition.
Means for solving the problems
In a first aspect, the present invention provides a pharmaceutical composition comprising a phenylpyrimidinone hydrochloride, comprising a compound of formula I-A, and a pharmaceutically acceptable carrier.
Wherein the particle size D of the compound of formula I-A90≤30μm。
Preferably, the particle size D of the compound of formula I-A90≤20μm。
Preferably, the pharmaceutically acceptable carrier includes a filler, a disintegrant, a binder, and a lubricant.
More preferably, the pharmaceutically acceptable carrier consists of a filler, a disintegrant, a binder and a lubricant.
Preferably, the pharmaceutical composition comprises the following components in percentage by weight: 1-20% of a compound of formula I-A, 35-90% of a filler, 1-20% of a disintegrating agent, 1-20% of an adhesive and 0.1-5% of a lubricant.
More preferably, the pharmaceutical composition comprises the following components in percentage by weight: 1-10% of a compound of formula I-A, 72-90% of a filler, 1-8% of a disintegrating agent, 1-8% of an adhesive and 0.5-2% of a lubricant.
Preferably, the filler is at least one of lactose, corn starch, mannitol, sorbitol and microcrystalline cellulose, the disintegrant is at least one of low-substituted hydroxypropyl cellulose, croscarmellose sodium, carboxymethyl starch sodium and crospovidone, the binder is at least one of hydroxypropyl cellulose, hydroxypropyl methylcellulose and povidone, and the lubricant is at least one of magnesium stearate, sodium stearyl fumarate, talc and colloidal silicon dioxide.
More preferably, the filler is lactose and microcrystalline cellulose, the disintegrant is carboxymethyl starch sodium, the binder is povidone, and the lubricant is magnesium stearate.
In a second aspect, the present invention provides a method for preparing the above pharmaceutical composition, which comprises the following steps: mixing a compound of formula I-A and a pharmaceutically acceptable carrier.
In a third aspect, the invention provides a pharmaceutical preparation, which is prepared from the pharmaceutical composition.
Preferably, the pharmaceutical preparation is a tablet, a capsule, a granule, a pill, a powder or a dry suspension.
More preferably, the pharmaceutical formulation is a tablet or capsule.
In a fourth aspect, the present invention provides a method for preparing the above pharmaceutical preparation, wherein the method can be selected from direct mixing, wet granulation or dry granulation, and preferably from direct mixing.
The preparation method comprises the following steps:
(1) pulverizing the compound of formula I-A to a target particle size, sieving the filler, disintegrant, binder and lubricant;
(2) uniformly mixing the compound of formula I-A crushed in the step (1) and the sieved filler, disintegrant and adhesive to obtain a mixed material; or
Uniformly mixing the compound of formula I-A crushed in the step (1) with the sieved filler and disintegrant, and adding the sieved adhesive solution in the step (1) for granulation to obtain drug-containing granules;
(3) adding the lubricant sieved in the step (1) into the mixed material or the medicine-containing granules in the step (2), and uniformly mixing to obtain total mixed powder;
(4) and (4) tabletting or filling the total mixed powder in the step (3) into capsules.
Preferably, the filler, disintegrant, binder and lubricant in step (1) are sieved through an 80 mesh sieve.
Preferably, step (4) further comprises a step of coating after tabletting.
In a fifth aspect, the invention provides the use of a pharmaceutical composition as described above or a pharmaceutical formulation as described above in the manufacture of a medicament for the treatment and/or prevention of a disease and/or condition associated with the PDE5 enzyme.
Preferably, the disease and/or condition associated with the PDE5 enzyme comprises: erectile dysfunction, pulmonary hypertension, female sexual dysfunction, premature labor, dysmenorrhea, benign prostatic hyperplasia, bladder outlet obstruction, incontinence, unstable and variant angina, hypertension, congestive heart failure, renal failure, atherosclerosis, stroke, peripheral vascular disease, raynaud's disease, inflammatory diseases, bronchitis, chronic asthma, allergic rhinitis, glaucoma, and disorders of bowel movement.
ADVANTAGEOUS EFFECTS OF INVENTION
The invention provides a pharmaceutical composition containing phenylpyrimidinone hydrochloride, a pharmaceutical preparation containing the same, a preparation method and application of the pharmaceutical composition, wherein the composition specifically comprises a compound shown in a formula I-A and a pharmaceutically acceptable carrier. The problems of mixing uniformity, content uniformity and slow dissolution are solved by limiting the granularity of the compound shown in the formula I-A, combining auxiliary materials and screening the dosage and carrying out a large number of experimental researches on the preparation process. The pharmaceutical composition or the pharmaceutical preparation has good content uniformity, good stability and rapid disintegration, can realize rapid dissolution, can be prepared by adopting two processes of direct mixing or wet granulation, preferentially adopts the direct mixing process, and has the characteristics of simple prescription process, low cost, energy conservation, environmental protection, easy industrial application and the like.
Detailed Description
[ definition of terms ]
Phenylpyrimidinone hydrochloride
The 'phenyl pyrimidone compound' is a compound with a phenyl pyrimidone structure, and a Chinese granted patent with the publication number of CN102216279B discloses a phenyl pyrimidone compound and pharmaceutically acceptable salts thereof, which have higher phosphodiesterase (PDE5) inhibition activity and better comprehensive pharmaceutical evaluation than sildenafil. "phenylpyrimidinone hydrochloride" refers to the hydrochloride salt of a phenylpyrimidinone compound.
Compounds of formula I-A
The compound of the formula I-A is hydrochloride of a phenyl pyrimidone compound, and has the following structure and the chemical name: 5, 6-diethyl-2- [ 2-n-propoxy-5- (2- (4-methylpiperazin-1-yl) acetamido) phenyl ] pyrimidin-4 (3H) -one hydrochloride.
Pharmaceutically acceptable carriers
By "pharmaceutically acceptable carrier" is meant a pharmaceutical excipient that is compatible with the pharmaceutically active ingredient and not deleterious to the subject, including, but not limited to, fillers, binders, disintegrants, lubricants, wetting agents, thickening agents, glidants, flavoring agents, olfactory agents, preservatives, antioxidants, pH adjusters, solvents, cosolvents, surfactants, and the like.
[ pharmaceutical composition ]
The invention provides a pharmaceutical composition containing phenylpyrimidinone hydrochloride, which comprises a compound shown as a formula I-A and a pharmaceutically acceptable carrier.
In one embodiment, the particle size D of the compound of formula I-A90≤30μm。
In a preferred embodiment, the particle size D of the compound of formula I-A90≤20μm。
In one embodiment, the pharmaceutically acceptable carrier includes a filler, a disintegrant, a binder, and a lubricant.
In a preferred embodiment, the pharmaceutically acceptable carrier consists of a filler, a disintegrant, a binder and a lubricant.
In one embodiment, the pharmaceutical composition comprises the following components in weight percent: 1-20% of a compound of formula I-A, 35-90% of a filler, 1-20% of a disintegrating agent, 1-20% of an adhesive and 0.1-5% of a lubricant.
In a preferred embodiment, the pharmaceutical composition comprises the following components in weight percent: 1-10% of a compound of formula I-A, 72-90% of a filler, 1-8% of a disintegrating agent, 1-8% of an adhesive and 0.5-2% of a lubricant.
In one embodiment, the filler is at least one of lactose, corn starch, mannitol, sorbitol, and microcrystalline cellulose, the disintegrant is at least one of low-substituted hydroxypropyl cellulose, croscarmellose sodium, carboxymethyl starch sodium, and crospovidone, the binder is at least one of hydroxypropyl cellulose, hydroxypropyl methylcellulose, and povidone, and the lubricant is at least one of magnesium stearate, sodium stearyl fumarate, talc, and colloidal silicon dioxide.
In a preferred embodiment, the fillers are lactose and microcrystalline cellulose, the disintegrant is sodium starch glycolate, the binder is povidone, and the lubricant is magnesium stearate.
[ Process for producing pharmaceutical composition ]
The invention provides a preparation method of the pharmaceutical composition, which comprises the following steps: mixing a compound of formula I-A and a pharmaceutically acceptable carrier.
[ pharmaceutical preparations ]
The invention provides a pharmaceutical preparation, which is prepared from the pharmaceutical composition.
In one embodiment, the pharmaceutical formulation is a tablet, capsule, granule, pill, powder, or dry suspension.
In a preferred embodiment, the pharmaceutical formulation is a tablet or capsule.
[ Process for producing pharmaceutical preparation ]
The invention provides a preparation method of the pharmaceutical preparation, which can select a preparation method of direct mixing, wet granulation or dry granulation, and preferably a preparation method of direct mixing.
The preparation method comprises the following steps:
(1) pulverizing the compound of formula I-A to a target particle size, sieving the filler, disintegrant, binder and lubricant;
(2) uniformly mixing the compound of formula I-A crushed in the step (1) and the sieved filler, disintegrant and adhesive to obtain a mixed material; or
Uniformly mixing the compound of formula I-A crushed in the step (1) with the sieved filler and disintegrant, and adding the sieved adhesive solution in the step (1) for granulation to obtain drug-containing granules;
(3) adding the lubricant sieved in the step (1) into the mixed material or the medicine-containing granules in the step (2), and uniformly mixing to obtain total mixed powder;
(4) and (4) tabletting or filling the total mixed powder in the step (3) into capsules.
In one embodiment, the filler, disintegrant, binder and lubricant in step (1) are sieved through an 80 mesh sieve.
In one embodiment, step (4) further comprises the step of coating after tableting.
[ medical use ]
The invention provides the application of the pharmaceutical composition or the pharmaceutical preparation in preparing medicines for treating and/or preventing diseases and/or symptoms related to PDE5 enzyme.
In one embodiment, the disease and/or condition associated with the PDE5 enzyme comprises: erectile dysfunction, pulmonary hypertension, female sexual dysfunction, premature labor, dysmenorrhea, benign prostatic hyperplasia, bladder outlet obstruction, incontinence, unstable and variant angina, hypertension, congestive heart failure, renal failure, atherosclerosis, stroke, peripheral vascular disease, raynaud's disease, inflammatory diseases, bronchitis, chronic asthma, allergic rhinitis, glaucoma, and disorders of bowel movement.
The present invention will be described in further detail below with reference to examples. It should not be understood that the scope of the above-described subject matter of the present invention is limited to the following examples. Various substitutions and alterations according to the general knowledge and conventional practice in the art are intended to be included within the scope of the present invention without departing from the technical spirit of the present invention as described above.
The method for detecting evaluation indexes such as disintegration time limit, friability, mixing uniformity, content uniformity, dissolution curve, appearance, powder flowability and the like in the embodiment or specific example of the present invention is as follows:
disintegration time limit: by adopting a method for checking the disintegration time limit of 0921 in the '2020 edition of Chinese pharmacopoeia', the tablet can be completely disintegrated in 900ml of water at 37 +/-1 ℃ within 30 minutes and passes through a screen, and if a small amount of light matter floats upwards or is adhered to a stainless steel pipe or the screen, but no hard core exists, the tablet can be taken as meeting the regulation theory. And (4) repeatedly measuring 6 pieces, wherein all the pieces meet the requirements, and if one piece does not meet the requirements, taking another 6 pieces for retesting, wherein all the pieces meet the requirements.
Friability: the method comprises the steps of adopting a tablet friability checking method of 0923 in 'Chinese pharmacopoeia' 2020 edition, using a tablet friability tester, taking a plurality of tablets to enable the total weight of the tablets to be about 6.5g, blowing off powder falling off from the tablets by using a blower, precisely weighing the tablets, placing the tablets in a cylinder, rotating the cylinders for 100 times, taking out the tablets, removing the powder by the same method, precisely weighing the tablets until the weight loss is less than 1%, and not checking the broken, cracked and crushed tablets. If the weight loss exceeds 1%, the weight loss should be measured 2 times, and the average weight loss of 3 times should not exceed 1%, and no fracture, crack or crushed piece should be detected.
Mixing uniformity: the content detection method is adopted, 10 mixed medicinal powders at different positions are taken, the content is detected, and the RSD value is calculated according to the content result, wherein the RSD value is generally considered to be less than 5 percent, so that the requirement of mixing uniformity is met.
Content uniformity: a content detection method is adopted, the content of a single measurement unit material amount (no less than 10 sampling points) is respectively detected, an A +2.2S value is calculated according to a content result, generally, the A +2.2 is considered to be less than 15, and the requirement of content uniformity is met.
Dissolution: the second method of 0931 dissolution and release determination method is adopted in 'Chinese pharmacopoeia' 2020 edition, and 0.1mol/L hydrochloric acid solution is adopted as dissolution medium, and the sampling time is as follows: 5. 10, 15, 30, 45min, medium volume 900ml, rotation speed: dissolution was measured at 50rpm, with the limits required: the amount eluted in 45 minutes should be not less than 80% of the indicated amount.
Plain sheet appearance: by adopting the contents of the general rule of 'Chinese pharmacopoeia' 2020 edition, 0101 tablet preparation, the plain tablet has complete and smooth appearance, uniform color, no sticking and uncovering, and proper hardness and wear resistance, so that the plain tablet is prevented from being worn and broken in the packaging and transportation processes.
Powder flowability: the common angle of repose indicates that the angle of repose is the maximum angle formed by the free slope of the powder accumulation layer and the horizontal plane, the smaller the angle of repose is, the smaller the friction force is, the better the fluidity is when the angle of repose is less than 30 degrees, and the fluidity requirement in the production process can be met when the angle of repose is less than 40 degrees. And >40 deg., the flowability requirement in the production process is generally considered to be not satisfied.
In order to solve the technical problems of small-dose medicine mixing uniformity, content uniformity and the like, the invention screens the use amount of auxiliary materials such as a filling agent, a disintegrating agent, an adhesive and the like and researches a large number of preparation process experiments, and inspects the indexes of the mixing uniformity, the content uniformity, the disintegration time limit, the friability, the powder flowability, the plain tablet appearance and the like of the pharmaceutical composition containing the phenyl pyrimidone hydrochloride.
The following examples are not specifically illustrated, and all starting materials and reagents are commercially available or prepared by conventional methods in the art. Wherein the compounds of formula I-A are purchased from Shandong Tei enamel pharmaceutical Co., Ltd, lactose (trade designations: G200, F100) is purchased from Deltakutazeugo Dairy, Germany, microcrystalline cellulose (trade designations: PH101, PH102) is purchased from Asahi Kasei-Kasei corporation, carboxymethyl starch sodium (trade designation: ZW-SSG-D) is purchased from Huzhou Yongyasu pharmaceutical Co., Ltd, povidone (trade designation: polyvinylpyrrolidone, trade designation: K30) is purchased from U.S. Pasteur Co., Ltd, starch, magnesium stearate (trade designation: SH-YM-M) is purchased from Anhui Shanhe pharmaceutical excipients Co., Ltd, film coating agents (trade designation: Opadry YS-1-7027CN) are purchased from Shanghai Kalerkang coating technology Co., Ltd, and gelatin hollow capsule shells (trade designations: 1#, 2#) are purchased from Suzhou capsule Co., Ltd.
Example 1: tablet formulation (direct compression)
The preparation process comprises the following steps:
(1) material pretreatment: pulverizing the compound of formula I-A, and determining the particle size D9018.8 μm; the auxiliary materials are sieved by a 80-mesh sieve for standby.
(2) Weighing: weighing the compound of formula I-A, lactose, microcrystalline cellulose, carboxymethyl starch sodium, polyvidone and magnesium stearate according to the prescription amount.
(3) Mixing: the components other than magnesium stearate were added to the hopper mixer at a rotation speed of 10rpm/min and mixed for 10 minutes.
(4) Lubrication: adding magnesium stearate, setting the rotating speed to be 10rpm/min, and mixing for 5 minutes to obtain total mixed powder; a total of 10 spots were sampled at different locations of the mixer to determine the uniformity of mixing. The particle content was measured and the tablet weight was calculated.
(5) Tabletting: tabletting by adopting a rotary tablet press, and tabletting a mould: the 6.5mm circular shallow concave punching die is controlled in the hardness range of 40-80N, the weight of the tablet is about 125mg, the weight difference limit is +/-5.0%, and sampling is carried out to determine the friability, the content and the like.
(6) Coating: adopting a film coating premix (Opadry YS-1-7027CN), weighing coating powder with a quantity of 4.0% of the single-pot quantity of the tablet core, adding the coating powder into purified water, stirring and dispersing uniformly to prepare a 15% (w/w) coating solution; and (3) placing the tablet core into a coating pot, setting the air inlet temperature to be 55-65 ℃, controlling the material temperature to be 40-60 ℃, setting the rotating speed of the pot body to be 1-10 rpm/min, and performing coating operation according to a coating program to control the coating weight to be increased by 1-3%.
Example 2: tablet formulation (Wet granulation)
The preparation process comprises the following steps:
(1) material pretreatment: pulverizing the compound of formula I-A, and determining the particle size D9018.8 μm; the auxiliary materials are sieved by a 80-mesh sieve for standby.
(2) Weighing: weighing the compound of formula I-A, lactose, microcrystalline cellulose, carboxymethyl starch sodium, polyvidone and magnesium stearate according to the prescription amount.
(3) Preparing a binder solution: the povidone K30 with the prescription amount is added into the 50 percent ethanol solution and stirred continuously to prepare clear 5 percent (w/w) povidone ethanol solution for standby.
(3) Premixing: adding other components except magnesium stearate into high speed wet granulating machine, stirring at 180rpm/min, and mixing for 10 min.
(4) And (3) granulating: setting the stirring speed of 180rpm/min and the shearing speed of 1200rpm/min, adding the adhesive solution for granulation, controlling the slurry adding time within 5min, setting the stirring speed of 180rpm/min and the shearing speed of 2000pm/min after the slurry adding is finished, and stirring for 5 min.
(5) Wet granulation: wet-granulating the granulated material by a swinging granulator (20-mesh screen).
(6) And (3) drying: adding the wet material into a boiling dryer, controlling the air inlet temperature at 60 ℃, and drying until the moisture is below 3.0% (measured by a halogen rapid moisture meter, 105 ℃/5 min).
(7) Dry granulation: and (3) carrying out dry granulation on the dried material by a crushing and granulating machine (granulation rotating speed is 1000rpm/min, and a V-shaped screen is 2.0 mm).
(8) Lubrication: adding magnesium stearate, setting the rotating speed to be 10rpm/min, and mixing for 5 minutes to obtain total mixed powder; a total of 10 spots were sampled at different locations of the mixer to determine the uniformity of mixing. The particle content was measured and the tablet weight was calculated.
(9) Tabletting: tabletting by adopting a rotary tablet press, and tabletting a mould: and (3) carrying out 6.5mm circular shallow concave punching, controlling the hardness range to be 40-80N, controlling the weight of the tablet to be about 125mg, and measuring the friability, the content and the like by sampling, wherein the weight difference limit is +/-5.0%.
(10) Coating: adopting a film coating premix (Opadry YS-1-7027CN), weighing coating powder with a quantity of 4.0% of the single-pot quantity of the tablet core, adding the coating powder into purified water, stirring and dispersing uniformly to prepare a 15% (w/w) coating solution; and (3) placing the tablet core into a coating pot, setting the air inlet temperature to be 55-65 ℃, controlling the material temperature to be 40-60 ℃, setting the rotating speed of the pot body to be 1-10 rpm/min, and performing coating operation according to a coating program to control the coating weight to be increased by 1-3%.
Example 3: tablet formulation (direct compression)
The preparation process is the same as in example 1.
Example 4: capsule prescription (direct mixing)
The process before capsule filling is the same as that of example 1, and the capsule filling steps are as follows: filling the capsule with No. 2 capsule by using a capsule filling plate, wherein the average filling weight is about 125 mg; and monitoring the product characters and weight difference in the filling process. The capsule properties are as follows: removing capsule shell to obtain white or quasi-white powder; limit of weight difference: 5.0 percent.
Example 5: capsule prescription (Wet granulation)
The process before capsule filling was the same as example 2, capsule filling: filling the capsule with No. 2 capsule by using a capsule filling plate, wherein the average filling weight is about 125 mg; and monitoring the product characters and weight difference in the filling process. The capsule properties are as follows: removing capsule shell to obtain white or quasi-white powder; limit of weight difference: 5.0 percent.
Example 6: capsule prescription (Wet granulation)
The prescription and the process design of the embodiment refer to the description of the granted patent (granted publication No. CN102216279B) at the 973-977 paragraph "the embodiment 222 capsule", and the preparation process is as follows: pulverizing the compound of formula I-A, and determining the particle size D9018.8 μm; sieving compound containing formula I-A and adjuvants such as starch, lactose and microcrystalline cellulose with 80 mesh sieve, weighing according to prescription, using 10% polyvinylpyrrolidone ethanol solution as binder, making into appropriate granule with 16 mesh sieve, drying at 65 deg.C, grading with 14 mesh sieve, adding magnesium stearate, and mixingAnd (3) homogenizing, measuring the content of the particles, calculating the filling amount, and filling into capsules (the average filling weight is 198mg) by using No. 1 capsules.
Example 7: tablet formulation (Wet granulation)
The prescription and the process design of the embodiment refer to the specification of the granted patent (granted publication No: CN102216279B) No. 978-980 paragraph "tablet of the embodiment 223 (wet granulation method)", and the preparation process is as follows: pulverizing the compound of formula I-A, and determining the particle size D9018.8 μm; sieving a compound containing the formula I-A and auxiliary materials of lactose, microcrystalline cellulose and sodium carboxymethyl starch by a sieve of 80 meshes, weighing according to the prescription amount, preparing a soft material by using 8% starch slurry, granulating by using a sieve of 16 meshes, drying, finishing granules, adding magnesium stearate, uniformly mixing, measuring the content of the granules, calculating the weight of the tablets, and tabletting (8.0 mm circular shallow concave punch die is adopted for tabletting, the hardness interval is controlled to be 60-100N, and the average value of the weight of the tablets is about 200 mg).
Example 8: tablet formulation (direct compression)
The preparation process is similar to example 1 except that the disintegrant and binder of example 8 are crospovidone and hydroxypropylcellulose.
Comparative example 1: tablet formulation (direct compression)
The preparation process is the same as example 1, except that: comparative example 1 Using the Compound of formula I-A without comminution treatment (found value: D)9088 μm) was prepared.
Comparative example 2: capsule prescription (Wet granulation)
The preparation process is the same as example 6, except that: comparative example 2 Using the Compound of formula I-A without pulverization treatment (found value: D)9088 μm) was prepared.
And (3) crystal form detection:
the crystal forms of the compound of formula I-A (not crushed), the compound of formula I-A (crushed) and the compound of formula I-A (simulated wet granulation, wetting by adding a small amount of solvent and drying) are determined by an X-ray powder diffraction method, and the XRPD patterns are respectively shown in figure 1, figure 2 and figure 3. The XRPD crystal form pattern shows that the compound of the formula I-A has stable crystal form and does not generate crystal form transformation in the process of crushing or simulating wet granulation, and the compound is supposed to have ideal stability in the subsequent preparation process.
Evaluation results table 1:
evaluation results table 2:
evaluation results table 3:
note: in the above 3 evaluation result tables, CR means a cumulative elution rate (cumulative release rate).
And (4) analyzing results:
the specific auxiliary material combination is adopted in the examples 1-8, the prepared tablet or capsule has good disintegration effect, and complete disintegration can be realized within 30 min. The auxiliary material combination of the examples 1 to 5 has better disintegration effect compared with the examples 6 to 8, complete disintegration can be realized within 10min, the examples 1 to 5 can realize rapid dissolution, and the examples 6 to 8 have slower dissolution.
The raw materials used in examples 1-8 were all mechanically crushed to control the particle size D of the material90Less than or equal to 30 mu m (measured value is D)9018.8 mu m), the prepared total mixed powder of the materials has better mixing uniformity and finished product content uniformity; comparative examples 1-2 use an unpulverized crude drug (found D)9088 μm) is directly mixed or wet granulated, and the flowability, mixing uniformity and content uniformity of the finished product of the material powder are relatively poor.
The flowability and compressibility of the intermediate powder in the two processes of direct mixing and wet granulation in examples 1 to 5 are all in accordance with requirements, the disintegration effect and dissolution behavior of each process are almost the same, the difference is small, the weight difference/loading difference, the content and the content uniformity are all in accordance with requirements, and the process steps are simple, special production conditions and production equipment are not needed, the cost is low, and the method is suitable for industrial production. The two processes are preferably direct mixing processes, so that the steps of wet granulation, drying, dry granulation and the like are reduced, the operation is simpler and more convenient, the environment protection, energy conservation and emission reduction are facilitated, and the method is more suitable for industrial production.