WO2018223895A1 - Long-acting sustained-release preparation of drug against parkinson's disease and preparation method thereof - Google Patents

Long-acting sustained-release preparation of drug against parkinson's disease and preparation method thereof Download PDF

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WO2018223895A1
WO2018223895A1 PCT/CN2018/089384 CN2018089384W WO2018223895A1 WO 2018223895 A1 WO2018223895 A1 WO 2018223895A1 CN 2018089384 W CN2018089384 W CN 2018089384W WO 2018223895 A1 WO2018223895 A1 WO 2018223895A1
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microspheres
release
long
sustained
release preparation
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PCT/CN2018/089384
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French (fr)
Chinese (zh)
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郑阳
赖树挺
曹付春
连远发
刘锋
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广州帝奇医药技术有限公司
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/5005Wall or coating material
    • A61K9/5021Organic macromolecular compounds
    • A61K9/5031Organic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyethylene glycol, poly(lactide-co-glycolide)
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/13Amines
    • A61K31/135Amines having aromatic rings, e.g. ketamine, nortriptyline
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/0002Galenical forms characterised by the drug release technique; Application systems commanded by energy
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/5084Mixtures of one or more drugs in different galenical forms, at least one of which being granules, microcapsules or (coated) microparticles according to A61K9/16 or A61K9/50, e.g. for obtaining a specific release pattern or for combining different drugs

Definitions

  • the invention belongs to the field of pharmacy, and particularly relates to a long-acting sustained-release preparation for anti-Parkinson's disease medicine and a preparation method thereof.
  • Rasagiline is a second-generation monoamine oxidase inhibitor that blocks the breakdown of the neurotransmitter dopamine, compared to first-generation monoamine oxidase inhibitors, including selegiline, sigrin, imipenem, and Jinsi.
  • the inhibitory effect is stronger, and it also has an effect on the patients whose long-term application of dopa preparations has a deteriorating effect.
  • the metabolite of rasagiline is an inactive non-amphetamine substance with small side effects and, more importantly, the drug has a certain symptom relief effect, and there is more evidence that these drugs have certain nerves. The role of protection.
  • Rasagiline currently has only oral tablets in the clinic. Although oral tablets are convenient to take, patients with Parkinson's disease often develop with nerve damage and memory loss, which leads to missed medication and the inability to regularly take drugs, leading to further deterioration of the disease. In addition, late Parkinson's patients often have difficulty swallowing and are not suitable for taking drugs. In addition, oral administration may have significant fluctuations in blood concentration, aggravating side effects, and appearing at the end of the agent and switching.
  • Patent CN 103494766 discloses a rasagiline oral disintegration composition, which solves the problem of difficulty in swallowing a drug, but cannot solve the problem of drug leakage and frequent medication.
  • Patent CN 1762495 discloses a preparation process of a long-acting sustained-release preparation for treating Parkinson's disease, using an organic solvent to dissolve a drug and a biodegradable medicinal polymer auxiliary, and injecting an organic solvent phase into a pharmaceutically acceptable water-soluble polymer.
  • the continuous aqueous phase forms microspheres, then volatilizes the organic solvent, and filters to obtain a sustained release microsphere, that is, an O/W process; or dissolves the drug and the biodegradable medicinal polymer auxiliary with an organic solvent, and then spray-drying Obtaining microspheres; or dissolving the drug and biodegradable medicinal polymer excipients in an organic solution with an organic solvent, spraying them into an organic non-solvent or water, and extracting them to form microspheres, ie, O/O Process or O/W process.
  • the drug is water-soluble, there is no protective measure and it is directly exposed to the external aqueous phase to lower the encapsulation efficiency, and therefore, it is difficult to obtain microspheres having a high content and a high encapsulation efficiency.
  • the use of the O/O process requires the use of a large amount of organic solvent, and requires the removal of all organic solvents used, and the process is complicated.
  • the first use of spray drying requires high temperature to cause degradation of raw materials, and the organic solvent spray drying requires explosion protection and has certain risks.
  • Patent CN 105769771 discloses a preparation method of an exenatide sustained-release microsphere composition, which first dissolves a drug substance using a strong polar solvent, then dissolves the polymer with a weakly polar solvent, and then adds a strong polar solvent. A suspension or a homogeneous solution is formed in the weakly polar solvent, and then added to the quencher to obtain fine particles.
  • the quenching agent is selected from the group consisting of silicone oil, liquid paraffin, mineral oil, requires a large amount of organic solvent, and needs to remove all the organic solvents used, and the process is complicated.
  • Patent CN 103338752 discloses a risperidone sustained release microsphere composition which discloses the use of two polymers of different viscosities to prepare microspheres for controlled release purposes, eliminating delayed release periods.
  • the use of two polymers without viscosity at the same time dissolved in an organic solvent and then the preparation of microspheres, on the one hand will increase the complexity of the prescription, different viscosity polymers may bring prescription compatibility problems, on the other hand, the method is applied in this
  • the invention also causes problems with product release.
  • Patent CN 104010629 discloses a triptorelin microsphere pharmaceutical composition which modulates release by adding glucose or mannitol to the microspheres to increase the initial release of the drug, thereby allowing the drug to function as quickly as possible.
  • the method of adding a release regulator also increases the complexity of the prescription on the one hand, and may bring about the problem of prescription compatibility.
  • the application of the method in the present invention also causes a problem of product release.
  • the present invention provides a rasagiline long-acting sustained-release composition and a preparation method thereof.
  • the invention improves the compliance of the rasagiline drug which is currently only administered orally in the clinical form, and improves the short release period and low drug loading of the sustained release microsphere preparation pharmaceutical composition disclosed in the prior literature, and No delayed release period.
  • the present inventors attempted to prepare rasagiline as a sustained-release microsphere with a longer release period according to the presently disclosed technical data, and replace the 50/65/35-100/0 PLGA with the technical means commonly used by those skilled in the art.
  • a PLGA of 50 found that the release period of the microspheres could be prolonged, but it was found that the microspheres showed a delayed release period.
  • the inventors have found that within the conventional particle size range of microspheres, as the particle size of the microspheres decreases, the microsphere release cycle and the delayed release period do become shorter, but the changes are not significant.
  • the inventors have creatively discovered that the preparation of microspheres into the nanometer to submicron level has resulted in significant changes in the release behavior of the microspheres. The first is that there is no delayed release period and no burst release, and the second is that the release cycle is significantly shortened. .
  • the inventors have spontaneously discovered that the release period of nano-to-submicron-sized microspheres is close to the delayed release period of ordinary particle size microspheres, even in some embodiments.
  • microspheres having a high drug loading amount and a high encapsulation ratio can be obtained.
  • the technical solution of the present invention is:
  • a long-acting sustained-release preparation for treating a Parkinson's disease drug the long-acting sustained-release preparation being a microsphere comprising rasagiline or a pharmaceutically acceptable salt thereof and biodegradable biocompatibility
  • a polymer comprising microspheres having an average particle diameter of 0.5 to 5 ⁇ m and microspheres having an average particle diameter of 20 to 150 ⁇ m.
  • microspheres having an average particle diameter of 0.5 to 5 ⁇ m account for 10 to 50% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 20 to 150 ⁇ m account for 50 to 90% by weight.
  • the microspheres having an average particle diameter of 0.5 to 5 ⁇ m account for 20 to 40% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 20 to 150 ⁇ m account for 60 to 80% by weight.
  • a long-acting sustained-release preparation for treating a Parkinson's disease drug the long-acting sustained-release preparation being a microsphere comprising rasagiline or a pharmaceutically acceptable salt thereof and a biodegradable organism
  • the microspheres preferably include microspheres having an average particle diameter of 0.5 to 3 ⁇ m and microspheres having an average particle diameter of 40 to 100 ⁇ m.
  • microspheres having an average particle diameter of 0.5 to 3 ⁇ m account for 10 to 50% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 40 to 100 ⁇ m account for 50 to 90% by weight.
  • the microspheres having an average particle diameter of 0.5 to 3 ⁇ m account for 20 to 40% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 40 to 100 ⁇ m account for 60 to 80% by weight.
  • rasagiline or a pharmaceutically acceptable salt thereof is from 10 to 50% by weight of the long-acting sustained release preparation.
  • a low-level drug may increase the total drug weight, and a high drug-loading amount may lower the encapsulation efficiency.
  • rasagiline or a pharmaceutically acceptable salt thereof accounts for 20-40% by weight of the long-acting sustained-release preparation. .
  • the biodegradable biocompatible polymer is poly(lactide-glycolide).
  • the molar ratio of lactide to glycolide is from 65:35 to 100:0.
  • the poly(lactide-glycolide) The preferred molar ratio of lactide to glycolide is from 70:30 to 95:5.
  • the poly(lactide-glycolide) More preferably, the molar ratio of lactide to glycolide is from 75:25 to 85:15.
  • the poly(lactide-glycolide) has a viscosity in the range of from 0.2 to 0.8 dl/g.
  • the poly(lactide-glycolide) has a viscosity in the range of from 0.3 to 0.6 dl/g.
  • the poly(lactide-glycolide) has a molecular weight ranging from 21 kDa to 89 kDa.
  • the terminal group of the poly(lactide-glycolide) is an ester group or a carboxyl group.
  • the terminal group of the poly(lactide-glycolide) is a carboxyl group.
  • the release period of the long-acting sustained-release preparation of the present invention is 4 to 12 weeks.
  • the invention further provides a preparation method of a long-acting sustained-release preparation for treating a Parkinson's disease medicine, comprising the following steps:
  • step c) the uniform solution B obtained in step b) is added to the homogeneous solution A obtained in step a) to obtain a uniform emulsion C;
  • the pharmaceutically acceptable water-soluble polymer is polyvinyl alcohol; the polyvinyl alcohol solution The concentration is from 0.5 to 4%; the continuous aqueous phase temperature is from 2 to 15 ° C, preferably 4 ° C.
  • step d) removing the organic solvent in the step d) microspheres, filtering, washing;
  • step f) The microspheres obtained in step e) are freeze-dried to obtain sustained-release microspheres.
  • the first type of organic solvent is selected from any one of dichloromethane, ethyl acetate, tetrahydrofuran, dimethyl sulfoxide, dimethylformamide or dimethylacetamide.
  • the second type of organic solvent is selected from any one of ethanol, acetic acid, hydrochloric acid, dimethyl sulfoxide, dimethylformamide or dimethylacetamide.
  • the first type of organic solvent is selected from any one of dichloromethane, ethyl acetate, and tetrahydrofuran.
  • the second type of organic solvent is selected from any one of ethanol, acetic acid, dimethyl sulfoxide, dimethylformamide or dimethylacetamide.
  • the first type of organic solvent is selected from the group consisting of dichloromethane.
  • the second type of organic solvent is selected from any one of ethanol and acetic acid.
  • step b) The solution obtained in step b) is added to step a) by sonication, vortexing, homogenization or stirring.
  • the uniform emulsion C obtained in the step c) is added to the continuous aqueous phase prepared by using the pharmaceutically acceptable water-soluble polymer by ultrasonication, vortexing, homogenization, high pressure homogenization or stirring.
  • the ultrasonic power is 200-400w
  • the vortex rotation speed is 2000-4000rpm
  • the homogenization speed is 4000-20000rpm
  • the high pressure homogenization is 600-1500bar
  • the stirring speed is 1000-3000rpm.
  • the ratio of the first type of organic solvent to the second type of organic solvent is from 2:1 to 20:1.
  • the ratio of the first type of organic solvent to the second type of organic solvent is from 2:1 to 10:1.
  • the pharmaceutical composition in the form of microspheres proposed by the present invention has the property of long-term release of drugs, and can release rasagiline in more than one month.
  • the present invention is characterized in that fluctuations in the concentration of rasagiline in plasma can be significantly reduced by using a suitable combination of two microparticles of different particle sizes in the pharmaceutical composition of the present invention without a significant delayed release period.
  • Another feature of the present invention is that in the case of a high drug loading amount, there is no drug burst phenomenon.
  • Figure 1 shows the release characteristics of the sustained release microspheres obtained in Example 1, Example 1-2, Example 1-4 and Example 1-6. It can be seen from the figure that within the ordinary particle size range, that is, 20- In the particle size range of 150 ⁇ m, although the release behavior of microspheres in different particle size ranges is different, it is not obvious;
  • Example 2 is a mixture of Example 1 sustained release microspheres (labeled as Example 1), Example 2 sustained release microspheres (labeled as Example 2), two parts of Example 1 and one example of Example 2 (labeled as an example) 1+2) in vitro release profile;
  • Figure 3 is a mixture of Example 3 sustained release microspheres (labeled as Example 3), Example 4 sustained release microspheres (labeled as Example 4), three parts of Example 1 and one example of Example 4 (labeled as examples) In vitro release profile of 3+4);
  • Figure 4 is a mixture of Example 5 sustained release microspheres (labeled as Example 5), Example 6 sustained release microspheres (labeled as Example 6), three of Example 5 and one of Example 6 (labeled as an example) In vitro release profile of 5+6);
  • Figure 5 is a mixture of Example 7 sustained release microspheres (labeled as Example 7), Example 8 sustained release microspheres (labeled as Example 8), two parts of Example 7 and one example of Example 8 (labeled as examples) In vitro release profile of 7+8).
  • Figure 6 is a mixture of Example 9 sustained release microspheres (labeled as Example 9), Example 10 sustained release microspheres (labeled as Example 10), five parts of Example 9 and a portion of Example 10 (labeled as examples) In vitro release profile of 9+10).
  • Figure 7 is a mixture of Example 11 sustained release microspheres (labeled as Example 11), Example 12 sustained release microspheres (labeled as Example 12), triplicate Example 11 and two Examples of Example 12 (labeled as examples) In vitro release profile of 11+12).
  • the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered to remove the continuous aqueous phase, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
  • 600g PLGA (85/15, 0.45dl/g, 51kDa, carboxyl end group) was dissolved in 60.00g of dichloromethane to obtain a uniform solution A; 4.00g of rasagiline was dissolved in 20.00g of ethanol to obtain a uniform solution B; Solution A was added to solution B under vortex conditions of 4000 rpm to obtain a uniform emulsion C.
  • the homogeneous solution C was added to a continuous aqueous phase of 1.5% polyvinyl alcohol at 4 ° C, and the microspheres were prepared by high pressure homogenization under a pressure of 1000 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
  • PLGA 100/0, 0.65 dl/g, 73 kDa, ester end group
  • a homogeneous solution A 5.00 g of rasagiline was dissolved in 25.00 g of dimethyl sulfoxide.
  • Uniform solution B under ultrasonic conditions, power 400w, solution A was added to solution B to obtain a uniform emulsion C.
  • the homogeneous solution C was added to a continuous aqueous phase of 0.5% polyvinyl alcohol at 4 ° C, and microspheres were prepared using mechanical stirring at 1000 rpm. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
  • PLGA 100/0, 0.45 dl/g, 53 kDa, carboxyl end group
  • a homogeneous solution A 5.00 g of rasagiline was dissolved in 25.00 g of dimethyl sulfoxide to obtain uniformity.
  • Solution B Solution A was added to Solution B under vortex conditions at 4000 rpm to obtain a homogeneous emulsion C.
  • the homogeneous solution C was added to a continuous aqueous phase of 1.5% polyvinyl alcohol at 4 ° C, and the microspheres were prepared by high pressure homogenization under a pressure of 1000 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
  • PLGA (85/15, 0.75dl/g, 81kDa, carboxyl end group) was dissolved in 150.00g of dichloromethane to obtain a homogeneous solution A; 3.50g of rasagiline was dissolved in 10.00g of acetic acid to obtain a uniform solution B; Solution A was added to solution B under vortex conditions of 2000 rpm to obtain a homogeneous emulsion C.
  • the homogeneous solution C was added to a continuous aqueous phase of 4.0% polyvinyl alcohol at 15 ° C, and microspheres were prepared using high pressure homogenization of 600 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
  • Example 1 87.5
  • Example 2 86.7
  • Example 3 89.3
  • Example 4 83.2
  • Example 5 90.5
  • Example 6 84.2
  • Example 7 89.5
  • Example 8 83.9
  • Example 9 90.3
  • Example 10 87.6
  • Example 11 91.5
  • Example 12 87.7
  • Example 14 Determination of particle size distribution of sustained release microspheres.
  • the particle size distribution of the microspheres was measured by a laser particle size tester.
  • the pump speed is 40%
  • the measurement time is 90s
  • the waiting time is 30s
  • the PIDS is set to "on”
  • the number of measurements is 1.
  • take appropriate amount of slow-release microspheres add 5-10 drops of 1% surfactant solution, then add 1ml of water and mix.
  • the instrument was turned on, and the sample was loaded into the sample cell until the opacity was 8-12%.
  • the measurement results were recorded, and the measurements were performed three times in parallel, and the average value was obtained. The results are shown in Table 2.
  • D10 represents that the number of microspheres smaller than the particle diameter accounts for 10% of the total amount
  • D50 represents the intermediate particle diameter, that is, the microspheres smaller than the particle diameter account for 50% of the total amount
  • D90 represents the number of microspheres smaller than the particle diameter. 90% of the total.
  • Example 1 38.64 70.21 113.88
  • Example 2 0.51 0.90 2.17
  • Example 3 29.53 74.07 118.68
  • Example 4 0.58 1.10 1.96
  • Example 5 35.34 81.05 138.05
  • Example 6 0.61 2.75 4.36
  • Example 7 27.46 60.57 112.89
  • Example 8 0.67 2.53 3.84
  • Example 9 23.17 40.31 60.08
  • Example 10 0.49 0.62 1.08
  • Example 11 65.89 108.4 145.79
  • Example 12 3.58 4.15 4.87
  • the slow-release microspheres were accurately weighed, and the acetonitrile-dispersed microspheres were added, and then the mobile phase of the triethylamine-glacial acetic acid buffer solution-acetonitrile (52:48) having a pH of 6.5 was dissolved and quantified to about 100 ⁇ g/ml.
  • Example 2 16.9 Example 3 28.7 Example 4 26.8 Example 5 37.4 Example 6 35.9 Example 7 45.6 Example 8 42.3 Example 9 38.7 Example 10 37.9 Example 11 34.7 Example 12 33.9
  • Example 16 Sustained release microsphere release characteristics.
  • Example 1-1 shows a 100-115 mesh microsphere obtained by sieving part of Example 1.
  • Example 1 The sustained-release microspheres prepared in Examples 1 to 12 and the microspheres sieved into different particle diameters in Example 1, that is, Example 1-2, Example 1-4, and Example 1-6, were released in vitro.
  • Test method Microspheres (30 mg) were accurately weighed, and 100 ml of PBS having a pH of 7.4 was added as a release medium, and a release experiment was carried out in a 37 ° C water bath shaker. The shaker was rotated at 100 rpm. At a fixed time, the sample was taken out and allowed to stand, and then the supernatant was passed through a 0.45 ⁇ m microporous membrane while fresh release medium was added and the content was determined by HPLC. Each batch of microspheres was run in triplicate. The release data is shown in Table 5, Table 6, and Figures 1 to 7 below.
  • Example 1 According to the release behaviors of Example 1, Example 3, Example 5, Example 7, Example 9, and Example 11, it can be seen that the microsphere release period is longer in the range of the ordinary particle size, that is, between 20 and 150 ⁇ m. A delayed release period occurs; by the release data of Example 2, Example 4, Example 6, Example 8, Example 10, and Example 12, it is known that the nanometer to submicron particle size range, that is, 0.5-5 micrometers During the period, the release period of the microspheres was short, but there was no delayed release period and no burst release.
  • Example 1 can be used in combination with Example 2.
  • the microspheres of Example 2 were responsible for the prophase release of the combination drug, and the microspheres of Example 1 were responsible for the later release. If the drug dosage required for the entire release cycle is 3 parts, then Example 1 provides two copies and Example 2 provides one portion.
  • Example 2 requires 10 mg of drug, ie 37.17 Mg microspheres; such as three parts of Example 3 mixed with one part of Example 4 (release cycle of about 5.7 weeks), three parts of Example 5 mixed with one part of Example 6 (release cycle of about 8.6 weeks), two implementations
  • Example 7 was mixed with one part of Example 8 (release cycle of about 12 weeks), five parts of Example 9 were mixed with one part of Example 8 (release cycle of about 6 weeks), and three parts of Example 11 were mixed with two parts of Example 12 ( The release period is about 7 weeks), and then an in vitro release test is performed, that is, a pharmaceutical composition having a release period of 4 to 12 weeks and no burst release and delayed release period can be obtained.
  • the premise of mixing is that the release period of the nano-submicron microspheres can just overlap with the delayed release period of the ordinary particle size microspheres.
  • Examples 2/4/6/8/10/12 correspond to the nano-to-submicron particle size microspheres of Example 1/3/5/7/9/11, respectively, which can achieve a longer release period and No purpose for a delayed release period.
  • this study found that within the conventional particle size range of the microspheres, as the particle size of the microspheres decreases, the microsphere release cycle and the delayed release period do become shorter, but the changes are not obvious.
  • the creative discovery found that the microspheres were prepared to a submicron level, and the microsphere release behavior changed significantly. The first was no delayed release period and no burst release, and the second was that the release cycle was significantly shortened.
  • the release period of the submicron-sized microspheres of the present invention is the same as that of the ordinary particle size microspheres.
  • microspheres with high drug loading and high encapsulation efficiency can be obtained by using the technical scheme, and the rasagiline in plasma can be significantly reduced by using a suitable combination of two microspheres of different particle sizes in the pharmaceutical composition of the invention. Fluctuations in concentration without significant delayed release. At the same time, in the case of high drug loading, the present invention has no sudden release of the drug.

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Abstract

A long-acting sustained-release preparation of a drug for treating Parkinson's disease and a preparation method thereof. The long-acting sustained-release preparation is microspheres comprising rasagiline or a pharmaceutically acceptable salt thereof and a biodegradable and biocompatible high molecular weight polymer. The microspheres comprise microspheres with an average particle size of 0.5-5 mm and microspheres with an average particle size of 20-150 mm.

Description

一种抗帕金森病药物的长效缓释制剂及其制备方法Long-acting sustained-release preparation for anti-Parkinson's disease medicine and preparation method thereof 技术领域Technical field
本发明属于制药领域,具体涉及一种抗帕金森病药物的长效缓释制剂及其制备方法。The invention belongs to the field of pharmacy, and particularly relates to a long-acting sustained-release preparation for anti-Parkinson's disease medicine and a preparation method thereof.
背景技术Background technique
雷沙吉兰是第二代单胺氧化酶抑制剂,能阻滞神经递质多巴胺的分解,与第一代单胺氧化酶抑制剂,包括司来吉兰、思吉宁、咪哆吡、金思平等相比,抑制作用更强,对长期应用多巴制剂药效出现衰退的患者也有改善的作用。另外,雷沙吉兰的代谢产物是一种无活性的非苯丙胺物质,副作用小,更重要的是,该药有一定的症状缓解的作用,并有较多证据证明这类药物有一定的神经保护的作用。Rasagiline is a second-generation monoamine oxidase inhibitor that blocks the breakdown of the neurotransmitter dopamine, compared to first-generation monoamine oxidase inhibitors, including selegiline, sigrin, imipenem, and Jinsi. The inhibitory effect is stronger, and it also has an effect on the patients whose long-term application of dopa preparations has a deteriorating effect. In addition, the metabolite of rasagiline is an inactive non-amphetamine substance with small side effects and, more importantly, the drug has a certain symptom relief effect, and there is more evidence that these drugs have certain nerves. The role of protection.
雷沙吉兰目前在临床上仅有口服片剂。口服片剂虽然服用方便,但帕金森病人随着病情的发展,往往伴有神经损伤,出现记忆力减退,从而导致漏服药物,无法规律服用药物,导致病情进一步恶化。再者帕金森后期患者常常具有吞咽困难,不适合服用药物。另外,口服给药会有明显的血药浓度波动,加重副作用,出现剂末现象和开关现象。Rasagiline currently has only oral tablets in the clinic. Although oral tablets are convenient to take, patients with Parkinson's disease often develop with nerve damage and memory loss, which leads to missed medication and the inability to regularly take drugs, leading to further deterioration of the disease. In addition, late Parkinson's patients often have difficulty swallowing and are not suitable for taking drugs. In addition, oral administration may have significant fluctuations in blood concentration, aggravating side effects, and appearing at the end of the agent and switching.
专利CN 103494766公开了一种雷沙吉兰经口崩解组合物,虽然解决了药品吞咽困难的问题,但是无法解决漏服药物,以及频繁用药等问题。Patent CN 103494766 discloses a rasagiline oral disintegration composition, which solves the problem of difficulty in swallowing a drug, but cannot solve the problem of drug leakage and frequent medication.
专利CN 1762495公开了一种治疗帕金森病的长效缓释制剂的制备工艺,使用有机溶剂把药物和生物可降解的药用高分子辅料溶解,将有机溶剂相注入到用药用水溶性高分子配制的连续水相中以形成微球,然后挥发掉有机溶剂,过滤得到缓释微球即O/W工艺;或用有机溶剂溶解药物和生物可降解的药用高分子辅料,然后采用喷雾干燥法制得微球;或用有机溶解剂把药物和生物可降解的药用高分子辅料充分溶解配制成有机溶液,将其喷雾至一有机非溶剂或水中,经萃取而制成微球即O/O工艺或O/W工艺。使用O/W工艺,由于药物是水溶性活性的,未有任何保护措施、会直接暴露在外部水相而降低包封率,因此,难以获取具有高含量和高包封率的微球。而使用O/O工艺,需要用到大量的有机溶剂,并且需要去除使用的全部有机溶剂,工艺复杂。使用喷雾干燥第一是需要有高温使原辅料造成降解,且有机溶剂喷雾干燥,需要防爆,有一定的危险性。Patent CN 1762495 discloses a preparation process of a long-acting sustained-release preparation for treating Parkinson's disease, using an organic solvent to dissolve a drug and a biodegradable medicinal polymer auxiliary, and injecting an organic solvent phase into a pharmaceutically acceptable water-soluble polymer. The continuous aqueous phase forms microspheres, then volatilizes the organic solvent, and filters to obtain a sustained release microsphere, that is, an O/W process; or dissolves the drug and the biodegradable medicinal polymer auxiliary with an organic solvent, and then spray-drying Obtaining microspheres; or dissolving the drug and biodegradable medicinal polymer excipients in an organic solution with an organic solvent, spraying them into an organic non-solvent or water, and extracting them to form microspheres, ie, O/O Process or O/W process. With the O/W process, since the drug is water-soluble, there is no protective measure and it is directly exposed to the external aqueous phase to lower the encapsulation efficiency, and therefore, it is difficult to obtain microspheres having a high content and a high encapsulation efficiency. The use of the O/O process requires the use of a large amount of organic solvent, and requires the removal of all organic solvents used, and the process is complicated. The first use of spray drying requires high temperature to cause degradation of raw materials, and the organic solvent spray drying requires explosion protection and has certain risks.
专利CN 105769771公开了一种艾塞那肽缓释微球组合物的制备方法,首先将原料药使用强极性溶剂溶解,然后将聚合物用弱极性溶剂溶解,然后将强极性溶剂加入弱极性溶剂中形成悬浊液或均一溶液,后加入淬灭剂中,得到微粒。其中淬灭剂选自硅油、液体石蜡、矿物油,需要用到大量的有机溶剂,并且需要去除使用的全部有机溶剂,工艺复杂。Patent CN 105769771 discloses a preparation method of an exenatide sustained-release microsphere composition, which first dissolves a drug substance using a strong polar solvent, then dissolves the polymer with a weakly polar solvent, and then adds a strong polar solvent. A suspension or a homogeneous solution is formed in the weakly polar solvent, and then added to the quencher to obtain fine particles. The quenching agent is selected from the group consisting of silicone oil, liquid paraffin, mineral oil, requires a large amount of organic solvent, and needs to remove all the organic solvents used, and the process is complicated.
M.Fernández等人的文献《Controlled release of rasagiline mesylate promotes neuroprotection in a rotenone-induced advanced model of Parkinson’s disease》公开了一种使用50/50 PLGA作为缓释材料,采用O/W和W/O/W工艺制备雷沙吉兰缓释微球的方法。但该方法制备得到微球释放周期较短,仅有两周,且药物的载药量较低,相同剂量下,注射的药物总量偏大,不利于患者的顺应性。The article "Controlled release of rasagiline mesylate promotes neuroprotection in a rotenone-induced advanced model of Parkinson's disease" by M. Fernández et al. discloses the use of 50/50 PLGA as a sustained release material using O/W and W/O/W. Process for preparing rasagiline sustained release microspheres. However, the microspheres prepared by the method have a short release period of only two weeks, and the drug loading amount is low. Under the same dose, the total amount of the injected drug is too large, which is unfavorable for patient compliance.
专利CN 103338752公开了一种利培酮缓释微球组合物,其公开了使用两种不同粘度的聚合物来制备微球,以此来达到调节释放目的,消除延迟释放期。但是使用两种不用粘度的聚合物同时溶于有机溶剂中然后制备微球,一方面会增加处方复杂性,不同粘度聚合物有可能带来处方相容性问题,另一方面该方法应用在本发明还会造成产品突释的问题。专利CN 104010629公开了一种曲普瑞林微球药物组合物,其通过在微球中添加葡萄糖或甘露醇来调节释放,提高药物的初始释放量,从而使药物尽快起效。但是使用添加释放调节剂的方法一方面同样增加处方复杂性,有可能带来处方相容性问题,另一方面该方法应用在本发明也还是会造成产品突释的问题。Patent CN 103338752 discloses a risperidone sustained release microsphere composition which discloses the use of two polymers of different viscosities to prepare microspheres for controlled release purposes, eliminating delayed release periods. However, the use of two polymers without viscosity at the same time dissolved in an organic solvent and then the preparation of microspheres, on the one hand will increase the complexity of the prescription, different viscosity polymers may bring prescription compatibility problems, on the other hand, the method is applied in this The invention also causes problems with product release. Patent CN 104010629 discloses a triptorelin microsphere pharmaceutical composition which modulates release by adding glucose or mannitol to the microspheres to increase the initial release of the drug, thereby allowing the drug to function as quickly as possible. However, the method of adding a release regulator also increases the complexity of the prescription on the one hand, and may bring about the problem of prescription compatibility. On the other hand, the application of the method in the present invention also causes a problem of product release.
发明内容Summary of the invention
发明目的:为解决现有技术中存在的问题,本发明提供一种雷沙吉兰长效缓释组合物及其制备方法。本发明改善了目前临床上只有口服形式进行给药的雷沙吉兰药物的依从性,并且改善了目前文献公开的缓释微球制剂药物组合物释放周期短,载药量低的缺点,且无延迟释放期。OBJECT OF THE INVENTION: To solve the problems in the prior art, the present invention provides a rasagiline long-acting sustained-release composition and a preparation method thereof. The invention improves the compliance of the rasagiline drug which is currently only administered orally in the clinical form, and improves the short release period and low drug loading of the sustained release microsphere preparation pharmaceutical composition disclosed in the prior literature, and No delayed release period.
本发明人按照目前公开的技术资料,尝试将雷沙吉兰制备成释放周期更长的缓释微球,按照本领域技术人员常用技术手段,使用65/35-100/0的PLGA替换50/50的PLGA,发现确实可以将微球的释放周期延长,但是发现,微球出现了延迟释放期。The present inventors attempted to prepare rasagiline as a sustained-release microsphere with a longer release period according to the presently disclosed technical data, and replace the 50/65/35-100/0 PLGA with the technical means commonly used by those skilled in the art. A PLGA of 50 found that the release period of the microspheres could be prolonged, but it was found that the microspheres showed a delayed release period.
在该领域,解决微球延迟释放期的常用技术有利用不同粘度型号的聚合物混合使用,以及添加释放调节剂等方法,但这些方法一个是均增加了处方复杂性,有可能带来处方相容性问题,另一个是,应用在本发明中会造成产品突释的问题。In this field, common techniques for solving the delayed release period of microspheres are the use of polymers of different viscosity types, as well as the addition of release modifiers, but each of these methods increases the complexity of the prescription and may lead to a prescription phase. The problem of capacitiveness, the other is that the application in the present invention causes a problem of product release.
另外本发明人发现在微球常规粒径范围内,随着微球粒径的减小,微球释放周期以及延迟释放期确实会变短,但是变化均不是明显的。但是本发明人却创造性的发现,将微球制备成纳米至亚微米级别,微球释放行为却发生了明显的改变,第一是无延迟释放期且无突释,第二是释放周期明显缩短。且本发明人奇迹的发现纳米至亚微米级别微球的释放期与普通粒径微球的延迟释放期接近,甚至在一些实施例中相同。In addition, the inventors have found that within the conventional particle size range of microspheres, as the particle size of the microspheres decreases, the microsphere release cycle and the delayed release period do become shorter, but the changes are not significant. However, the inventors have creatively discovered that the preparation of microspheres into the nanometer to submicron level has resulted in significant changes in the release behavior of the microspheres. The first is that there is no delayed release period and no burst release, and the second is that the release cycle is significantly shortened. . Moreover, the inventors have miraculously discovered that the release period of nano-to-submicron-sized microspheres is close to the delayed release period of ordinary particle size microspheres, even in some embodiments.
因此本发明人想到将两种不同粒径的微球混合使用,不仅可以得到释放周期较长的产品, 且无延迟释放期。Therefore, the inventors thought that mixing two kinds of microspheres of different particle diameters can not only obtain a product with a long release period, but also has no delayed release period.
另外本发明人实验发现,使用目前公知技术,无法得到高载药量和包封率的产品。但是按照本发明公开的技术,却能得到高载药量和高包封率的微球。Further, the inventors have experimentally found that a product having a high drug loading amount and an encapsulation ratio cannot be obtained by using a conventionally known technique. However, according to the technique disclosed in the present invention, microspheres having a high drug loading amount and a high encapsulation ratio can be obtained.
具体地,为实现本发明的技术目的,本发明的技术方案为:Specifically, in order to achieve the technical object of the present invention, the technical solution of the present invention is:
一种治疗帕金森病药物的长效缓释制剂,所述长效缓释制剂为微球,所述微球包含雷沙吉兰或其药物学可接受的盐和生物可降解生物相容性高分子,所述微球包括平均粒径为0.5-5μm的微球和平均粒径为20-150μm的微球。A long-acting sustained-release preparation for treating a Parkinson's disease drug, the long-acting sustained-release preparation being a microsphere comprising rasagiline or a pharmaceutically acceptable salt thereof and biodegradable biocompatibility A polymer comprising microspheres having an average particle diameter of 0.5 to 5 μm and microspheres having an average particle diameter of 20 to 150 μm.
所述平均粒径为0.5-5μm的微球占长效缓释制剂的10-50wt%,平均粒径为20-150μm的微球占50-90wt%。The microspheres having an average particle diameter of 0.5 to 5 μm account for 10 to 50% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 20 to 150 μm account for 50 to 90% by weight.
进一步优选地,所述平均粒径为0.5-5μm的微球占长效缓释制剂的20-40wt%,平均粒径为20-150μm的微球占60-80wt%。Further preferably, the microspheres having an average particle diameter of 0.5 to 5 μm account for 20 to 40% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 20 to 150 μm account for 60 to 80% by weight.
优选地,一种治疗帕金森病药物的长效缓释制剂,所述长效缓释制剂为微球,所述微球包含雷沙吉兰或其药物学可接受的盐和生物可降解生物相容性高分子,所述微球优选包括平均粒径为0.5-3μm的微球和平均粒径为40-100μm的微球。Preferably, a long-acting sustained-release preparation for treating a Parkinson's disease drug, the long-acting sustained-release preparation being a microsphere comprising rasagiline or a pharmaceutically acceptable salt thereof and a biodegradable organism As the compatible polymer, the microspheres preferably include microspheres having an average particle diameter of 0.5 to 3 μm and microspheres having an average particle diameter of 40 to 100 μm.
所述平均粒径为0.5-3μm的微球占长效缓释制剂的10-50wt%,平均粒径为40-100μm的微球占50-90wt%。The microspheres having an average particle diameter of 0.5 to 3 μm account for 10 to 50% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 40 to 100 μm account for 50 to 90% by weight.
进一步优选地,所述平均粒径为0.5-3μm的微球占长效缓释制剂的20-40wt%,平均粒径为40-100μm的微球占60-80wt%。Further preferably, the microspheres having an average particle diameter of 0.5 to 3 μm account for 20 to 40% by weight of the long-acting sustained-release preparation, and the microspheres having an average particle diameter of 40 to 100 μm account for 60 to 80% by weight.
优选地,雷沙吉兰或其药学上可接受的盐占长效缓释制剂的10-50wt%。Preferably, rasagiline or a pharmaceutically acceptable salt thereof is from 10 to 50% by weight of the long-acting sustained release preparation.
低含量药物会是使总给药重量增加,高载药量可能会包封率下降,进一步优选地,雷沙吉兰或其药学上可接受的盐占长效缓释制剂的20-40wt%。A low-level drug may increase the total drug weight, and a high drug-loading amount may lower the encapsulation efficiency. Further preferably, rasagiline or a pharmaceutically acceptable salt thereof accounts for 20-40% by weight of the long-acting sustained-release preparation. .
在一种优选地实施方案中,所述生物可降解生物相容性高分子为聚(丙交酯-乙交酯)。In a preferred embodiment, the biodegradable biocompatible polymer is poly(lactide-glycolide).
进一步优选地,所述聚(丙交酯-乙交酯)中,丙交酯和乙交酯的摩尔比为65:35~100:0。Further preferably, in the poly(lactide-glycolide), the molar ratio of lactide to glycolide is from 65:35 to 100:0.
在临床应用上,药物释放时间越长越好,但是更长时间可能会一次给药过多,不利于患者顺应性,因此在某些情况下,所述聚(丙交酯-乙交酯)中,丙交酯和乙交酯的优选摩尔比为70:30~95:5。In clinical applications, the longer the drug release time, the better, but it may be administered too much at a time, which is not conducive to patient compliance, so in some cases, the poly(lactide-glycolide) The preferred molar ratio of lactide to glycolide is from 70:30 to 95:5.
在临床应用上,药物释放时间越长越好,但是更长时间可能会一次给药过多,不利于患者顺应性,因此在某些情况下,所述聚(丙交酯-乙交酯)中,丙交酯和乙交酯的更优选摩尔比为75:25~85:15。In clinical applications, the longer the drug release time, the better, but it may be administered too much at a time, which is not conducive to patient compliance, so in some cases, the poly(lactide-glycolide) More preferably, the molar ratio of lactide to glycolide is from 75:25 to 85:15.
在一种优选地实施方案中,所述聚(丙交酯-乙交酯)的粘度范围为0.2-0.8dl/g。In a preferred embodiment, the poly(lactide-glycolide) has a viscosity in the range of from 0.2 to 0.8 dl/g.
进一步优选地,所述聚(丙交酯-乙交酯)的粘度范围为0.3-0.6dl/g。Further preferably, the poly(lactide-glycolide) has a viscosity in the range of from 0.3 to 0.6 dl/g.
在一种优选地实施方案中,所述聚(丙交酯-乙交酯)的分子量范围21kDa-89kDa。In a preferred embodiment, the poly(lactide-glycolide) has a molecular weight ranging from 21 kDa to 89 kDa.
在一种优选地实施方案中,所述聚(丙交酯-乙交酯)的末端基为酯基或羧基。In a preferred embodiment, the terminal group of the poly(lactide-glycolide) is an ester group or a carboxyl group.
进一步优选地,所述聚(丙交酯-乙交酯)的末端基为羧基。Further preferably, the terminal group of the poly(lactide-glycolide) is a carboxyl group.
本发明所述长效缓释制剂的释放周期在4~12周。The release period of the long-acting sustained-release preparation of the present invention is 4 to 12 weeks.
本发明进一步提出了一种治疗帕金森病药物的长效缓释制剂的制备方法,包括如下步骤:The invention further provides a preparation method of a long-acting sustained-release preparation for treating a Parkinson's disease medicine, comprising the following steps:
a)将生物可降解生物相容性高分子溶于第一类有机溶剂,得到均一溶液A;a) dissolving the biodegradable biocompatible polymer in the first type of organic solvent to obtain a uniform solution A;
b)将雷沙吉兰或其药物学可接受的盐溶于能与第一类有机溶剂互溶的第二类有机溶剂,得均一溶液B;b) rasagiline or a pharmaceutically acceptable salt thereof is dissolved in a second type of organic solvent which is miscible with the first type of organic solvent to obtain a homogeneous solution B;
c)将步骤b)得到的均一溶液B加入步骤a)得到的均一溶液A中得到均一乳液C;c) the uniform solution B obtained in step b) is added to the homogeneous solution A obtained in step a) to obtain a uniform emulsion C;
d)将步骤c)得到的均一乳液C加入用药用水溶性高分子配制的连续水相中以形成微球;优选地,所述药用水溶性高分子为聚乙烯醇;所述聚乙烯醇溶液浓度为0.5-4%;所述连续水相温度为2-15℃,优选4℃。d) adding the uniform emulsion C obtained in the step c) to the continuous aqueous phase prepared by using the pharmaceutically acceptable water-soluble polymer to form microspheres; preferably, the pharmaceutically acceptable water-soluble polymer is polyvinyl alcohol; the polyvinyl alcohol solution The concentration is from 0.5 to 4%; the continuous aqueous phase temperature is from 2 to 15 ° C, preferably 4 ° C.
e)去除步骤d)微球中的有机溶剂,过滤,洗涤;e) removing the organic solvent in the step d) microspheres, filtering, washing;
f)将步骤e)所得微球冷冻干燥,得到缓释微球。f) The microspheres obtained in step e) are freeze-dried to obtain sustained-release microspheres.
优选地,第一类有机溶剂选自二氯甲烷、乙酸乙酯、四氢呋喃、二甲基亚砜、二甲基甲酰胺或二甲基乙酰胺中的任意一种。第二类有机溶剂选自乙醇、乙酸、盐酸、二甲基亚砜、二甲基甲酰胺或二甲基乙酰胺中的任意一种。Preferably, the first type of organic solvent is selected from any one of dichloromethane, ethyl acetate, tetrahydrofuran, dimethyl sulfoxide, dimethylformamide or dimethylacetamide. The second type of organic solvent is selected from any one of ethanol, acetic acid, hydrochloric acid, dimethyl sulfoxide, dimethylformamide or dimethylacetamide.
进一步优选地,第一类有机溶剂选自二氯甲烷、乙酸乙酯、四氢呋喃中的任意一种。第二类有机溶剂选自乙醇、乙酸、二甲基亚砜、二甲基甲酰胺或二甲基乙酰胺中的任意一种。Further preferably, the first type of organic solvent is selected from any one of dichloromethane, ethyl acetate, and tetrahydrofuran. The second type of organic solvent is selected from any one of ethanol, acetic acid, dimethyl sulfoxide, dimethylformamide or dimethylacetamide.
更进一步优选地,第一类有机溶剂选自二氯甲烷。第二类有机溶剂选自乙醇、乙酸的任意一种。Still more preferably, the first type of organic solvent is selected from the group consisting of dichloromethane. The second type of organic solvent is selected from any one of ethanol and acetic acid.
将步骤b)得到的溶液在加入步骤a)时采用超声、涡旋、均质或搅拌方式。The solution obtained in step b) is added to step a) by sonication, vortexing, homogenization or stirring.
将步骤c)得到的均一乳液C加入用药用水溶性高分子配制的连续水相中时采用超声、涡旋、均质、高压均质或搅拌的方式。The uniform emulsion C obtained in the step c) is added to the continuous aqueous phase prepared by using the pharmaceutically acceptable water-soluble polymer by ultrasonication, vortexing, homogenization, high pressure homogenization or stirring.
其中超声功率在200-400w,涡旋转速在2000-4000rpm,均质速度在4000-20000rpm,高压均质在600-1500bar;搅拌速度在1000-3000rpm。The ultrasonic power is 200-400w, the vortex rotation speed is 2000-4000rpm, the homogenization speed is 4000-20000rpm, the high pressure homogenization is 600-1500bar, and the stirring speed is 1000-3000rpm.
优选的,第一类有机溶剂与第二类有机溶剂的比例为2:1-20:1。Preferably, the ratio of the first type of organic solvent to the second type of organic solvent is from 2:1 to 20:1.
进一步优选的,第一类有机溶剂与第二类有机溶剂的比例为2:1-10:1。Further preferably, the ratio of the first type of organic solvent to the second type of organic solvent is from 2:1 to 10:1.
有益效果:与现有技术相比,本发明提出的微球形式存在的药物组合物,具有药物长期释放的性质,可在超过一个月的时间里释放雷沙吉兰。本发明的特征在于通过在本发明的药物组合物中使用2种不同粒径微球的适宜组合,可以显著减少血浆中雷沙吉兰浓度的波动, 且无明显的延迟释放期。本发明的另一个特征是在载药量高的情况下,无药物突释现象。Advantageous Effects: Compared with the prior art, the pharmaceutical composition in the form of microspheres proposed by the present invention has the property of long-term release of drugs, and can release rasagiline in more than one month. The present invention is characterized in that fluctuations in the concentration of rasagiline in plasma can be significantly reduced by using a suitable combination of two microparticles of different particle sizes in the pharmaceutical composition of the present invention without a significant delayed release period. Another feature of the present invention is that in the case of a high drug loading amount, there is no drug burst phenomenon.
附图说明DRAWINGS
图1为实施例1、实施例1-2、实施例1-4和实施例1-6所得缓释微球的释放特性,从图中可以看出,在普通粒径范围内,即20-150μm粒径范围内,虽然不同粒径范围微球释放行为有差异,但是并不明显;Figure 1 shows the release characteristics of the sustained release microspheres obtained in Example 1, Example 1-2, Example 1-4 and Example 1-6. It can be seen from the figure that within the ordinary particle size range, that is, 20- In the particle size range of 150 μm, although the release behavior of microspheres in different particle size ranges is different, it is not obvious;
图2为实施例1缓释微球(标注为实施例1)、实施例2缓释微球(标注为实施例2)、两份实施例1与一份实施例2混合物(标注为实施例1+2)的体外释放曲线;2 is a mixture of Example 1 sustained release microspheres (labeled as Example 1), Example 2 sustained release microspheres (labeled as Example 2), two parts of Example 1 and one example of Example 2 (labeled as an example) 1+2) in vitro release profile;
图3为实施例3缓释微球(标注为实施例3)、实施例4缓释微球(标注为实施例4)、三份实施例1与一份实施例4混合物(标注为实施例3+4)的体外释放曲线;Figure 3 is a mixture of Example 3 sustained release microspheres (labeled as Example 3), Example 4 sustained release microspheres (labeled as Example 4), three parts of Example 1 and one example of Example 4 (labeled as examples) In vitro release profile of 3+4);
图4为实施例5缓释微球(标注为实施例5)、实施例6缓释微球(标注为实施例6)、三份实施例5与一份实施例6混合物(标注为实施例5+6)的体外释放曲线;Figure 4 is a mixture of Example 5 sustained release microspheres (labeled as Example 5), Example 6 sustained release microspheres (labeled as Example 6), three of Example 5 and one of Example 6 (labeled as an example) In vitro release profile of 5+6);
图5为实施例7缓释微球(标注为实施例7)、实施例8缓释微球(标注为实施例8)、两份实施例7与一份实施例8混合物(标注为实施例7+8)的体外释放曲线。Figure 5 is a mixture of Example 7 sustained release microspheres (labeled as Example 7), Example 8 sustained release microspheres (labeled as Example 8), two parts of Example 7 and one example of Example 8 (labeled as examples) In vitro release profile of 7+8).
图6为实施例9缓释微球(标注为实施例9)、实施例10缓释微球(标注为实施例10)、五份实施例9与一份实施例10混合物(标注为实施例9+10)的体外释放曲线。Figure 6 is a mixture of Example 9 sustained release microspheres (labeled as Example 9), Example 10 sustained release microspheres (labeled as Example 10), five parts of Example 9 and a portion of Example 10 (labeled as examples) In vitro release profile of 9+10).
图7为实施例11缓释微球(标注为实施例11)、实施例12缓释微球(标注为实施例12)、三份实施例11与两份实施例12混合物(标注为实施例11+12)的体外释放曲线。Figure 7 is a mixture of Example 11 sustained release microspheres (labeled as Example 11), Example 12 sustained release microspheres (labeled as Example 12), triplicate Example 11 and two Examples of Example 12 (labeled as examples) In vitro release profile of 11+12).
具体实施方式detailed description
下面对本发明技术方案进行详细说明,但是本发明的保护范围不局限于所述实施例。The technical solution of the present invention will be described in detail below, but the scope of protection of the present invention is not limited to the embodiment.
实施例1.缓释微球制备。Example 1. Preparation of sustained release microspheres.
将8.00gPLGA(丙交酯/乙交酯=65/35,下文同,均为丙交酯/乙交酯,0.65dl/g,71kDa,酯基端基)溶于80.00g二氯甲烷,得均一溶液A;将2.00g雷沙吉兰溶于10.00g乙醇,得均一溶液B;在3000rpm的涡旋条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的1.0%的聚乙烯醇水溶液中,使用2000rpm的机械搅拌器搅拌制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。8.00 g of PLGA (lactide / glycolide = 65 / 35, the same below, are lactide / glycolide, 0.65dl / g, 71kDa, ester end groups) dissolved in 80.00g of dichloromethane, Uniform solution A; 2.00 g of rasagiline dissolved in 10.00 g of ethanol to obtain a homogeneous solution B; solution A was added to solution B under vortex conditions at 3000 rpm to obtain a uniform emulsion C. The homogeneous solution C was added to a 1.0% aqueous solution of polyvinyl alcohol at 4 ° C, and the microspheres were prepared by stirring using a mechanical stirrer at 2000 rpm. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例2.缓释微球的制备。Example 2. Preparation of sustained release microspheres.
将8.00g PLGA(65/35,0.65dl/g,71kDa,酯基端基)溶于80.00g二氯甲烷,得均一溶液A;将2.00g雷沙吉兰溶于10.00g乙醇,得均一溶液B;在超声条件下,功率300w,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的1.0%的聚乙烯醇连续水相中,在900bar的压力下高压均质制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球除去连续水相,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。8.00 g of PLGA (65/35, 0.65 dl/g, 71 kDa, ester end group) was dissolved in 80.00 g of dichloromethane to obtain a homogeneous solution A; 2.00 g of rasagiline was dissolved in 10.00 g of ethanol to obtain a homogeneous solution. B; under ultrasonic conditions, power 300w, solution A was added to solution B to obtain a uniform emulsion C. The homogeneous solution C was added to a 1.0% polyvinyl alcohol continuous aqueous phase at 4 ° C, and the microspheres were prepared by high pressure homogenization under a pressure of 900 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered to remove the continuous aqueous phase, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例3.缓释微球的制备。Example 3. Preparation of sustained release microspheres.
将7.00g PLGA(75/25,0.5dl/g,57kDa,羧基端基)溶于70.00g乙酸乙酯,得均一溶液A;将3.00g雷沙吉兰溶于15.00g乙酸,得均一溶液B;在3000rpm的涡旋条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的0.5%的聚乙烯醇连续水相中,使用4000rpm的均质机均质制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。7.00 g of PLGA (75/25, 0.5 dl/g, 57 kDa, carboxyl end group) was dissolved in 70.00 g of ethyl acetate to obtain a homogeneous solution A; 3.00 g of rasagiline was dissolved in 15.00 g of acetic acid to obtain a homogeneous solution B. Solution A was added to solution B under vortex conditions of 3000 rpm to obtain a uniform emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 0.5% polyvinyl alcohol at 4 ° C, and the microspheres were homogenized using a homogenizer at 4000 rpm. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例4.缓释微球的制备。Example 4. Preparation of sustained release microspheres.
将7.00g PLGA(75/25,0.5dl/g,57kDa,羧基端基)溶于70.00g乙酸乙酯,得均一溶液A;将3.00g雷沙吉兰溶于15.00g乙酸,得均一溶液B;在4000rpm的涡旋条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的0.5%的聚乙烯醇连续水相中,在1000bar的压力下高压均质制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。7.00 g of PLGA (75/25, 0.5 dl/g, 57 kDa, carboxyl end group) was dissolved in 70.00 g of ethyl acetate to obtain a homogeneous solution A; 3.00 g of rasagiline was dissolved in 15.00 g of acetic acid to obtain a homogeneous solution B. Solution A was added to solution B under vortex conditions at 4000 rpm to obtain a uniform emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 0.5% polyvinyl alcohol at 4 ° C, and the microspheres were prepared by high pressure homogenization under a pressure of 1000 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例5.缓释微球的制备。Example 5. Preparation of sustained release microspheres.
将6.00g PLGA(85/15,0.4dl/g,46kDa,羧基端基)溶于60.00g二氯甲烷,得均一溶液A;将4.00g雷沙吉兰溶于20.00g乙醇,得均一溶液B;在超声条件下,功率300w,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的0.5%的聚乙烯醇连续水相中,使用1000rpm的机械搅拌制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。6.00 g of PLGA (85/15, 0.4 dl/g, 46 kDa, carboxyl end group) was dissolved in 60.00 g of dichloromethane to obtain a homogeneous solution A; 4.00 g of rasagiline was dissolved in 20.00 g of ethanol to obtain a homogeneous solution B. Under ultrasonic conditions, power 300w, solution A was added to solution B to obtain a uniform emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 0.5% polyvinyl alcohol at 4 ° C, and microspheres were prepared using mechanical stirring at 1000 rpm. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例6.缓释微球的制备。Example 6. Preparation of sustained release microspheres.
将600g PLGA(85/15,0.45dl/g,51kDa,羧基端基)溶于60.00g二氯甲烷,得均一溶液A;将4.00g雷沙吉兰溶于20.00g乙醇,得均一溶液B;在4000rpm的涡旋条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的1.5%的聚乙烯醇连续水相中,在 1000bar的压力下高压均质制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。600g PLGA (85/15, 0.45dl/g, 51kDa, carboxyl end group) was dissolved in 60.00g of dichloromethane to obtain a uniform solution A; 4.00g of rasagiline was dissolved in 20.00g of ethanol to obtain a uniform solution B; Solution A was added to solution B under vortex conditions of 4000 rpm to obtain a uniform emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 1.5% polyvinyl alcohol at 4 ° C, and the microspheres were prepared by high pressure homogenization under a pressure of 1000 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例7.缓释微球的制备。Example 7. Preparation of sustained release microspheres.
将5.00g PLGA(100/0,0.65dl/g,73kDa,酯基端基)溶于50.00g四氢呋喃,得均一溶液A;将5.00g雷沙吉兰溶于25.00g二甲基亚砜,得均一溶液B;在超声条件下,功率400w,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的0.5%的聚乙烯醇连续水相中,使用1000rpm的机械搅拌制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。5.00 g of PLGA (100/0, 0.65 dl/g, 73 kDa, ester end group) was dissolved in 50.00 g of tetrahydrofuran to obtain a homogeneous solution A; 5.00 g of rasagiline was dissolved in 25.00 g of dimethyl sulfoxide. Uniform solution B; under ultrasonic conditions, power 400w, solution A was added to solution B to obtain a uniform emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 0.5% polyvinyl alcohol at 4 ° C, and microspheres were prepared using mechanical stirring at 1000 rpm. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例8.缓释微球的制备。Example 8. Preparation of sustained release microspheres.
将5.00g PLGA(100/0,0.45dl/g,53kDa,羧基端基)溶于50.00g四氢呋喃,得均一溶液A;将5.00g雷沙吉兰溶于25.00g二甲基亚砜,得均一溶液B;在4000rpm的涡旋条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入4℃的1.5%的聚乙烯醇连续水相中,在1000bar的压力下高压均质制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。5.00 g of PLGA (100/0, 0.45 dl/g, 53 kDa, carboxyl end group) was dissolved in 50.00 g of tetrahydrofuran to obtain a homogeneous solution A; 5.00 g of rasagiline was dissolved in 25.00 g of dimethyl sulfoxide to obtain uniformity. Solution B; Solution A was added to Solution B under vortex conditions at 4000 rpm to obtain a homogeneous emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 1.5% polyvinyl alcohol at 4 ° C, and the microspheres were prepared by high pressure homogenization under a pressure of 1000 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例9.缓释微球的制备。Example 9. Preparation of sustained release microspheres.
将6.00g PLGA(75/25,0.6dl/g,69kDa,酯基端基)溶于100.00g二甲基亚砜,得均一溶液A;将4.00g雷沙吉兰溶于10.00g二甲基甲酰胺,得均一溶液B;在2000rpm的机械搅拌条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入10℃的3.0%的聚乙烯醇连续水相中,使用1500rpm的机械搅拌制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。6.00 g of PLGA (75/25, 0.6 dl/g, 69 kDa, ester end group) was dissolved in 100.00 g of dimethyl sulfoxide to obtain a homogeneous solution A; 4.00 g of rasagiline was dissolved in 10.00 g of dimethyl group. Formamide was obtained as a homogeneous solution B; solution A was added to solution B under mechanical stirring at 2000 rpm to obtain a uniform emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 3.0% polyvinyl alcohol at 10 ° C, and microspheres were prepared using mechanical stirring at 1500 rpm. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例10.缓释微球的制备。Example 10. Preparation of sustained release microspheres.
将6.00g PLGA(65/35,0.5dl/g,58kDa,羧基端基)溶于150.00g二甲基甲酰胺,得均一溶液A;将4.00g雷沙吉兰溶于8.00g乙酸,得均一溶液B;在4000rpm的均质条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入10℃的3.0%的聚乙烯醇连续水相中,在10000rpm的高速均质条件下制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。6.00 g of PLGA (65/35, 0.5 dl/g, 58 kDa, carboxyl end group) was dissolved in 150.00 g of dimethylformamide to obtain a homogeneous solution A; 4.00 g of rasagiline was dissolved in 8.00 g of acetic acid to obtain uniformity. Solution B; Solution A was added to Solution B under homogeneous conditions of 4000 rpm to obtain a homogeneous emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 3.0% polyvinyl alcohol at 10 ° C, and microspheres were prepared under high-speed homogenization conditions of 10,000 rpm. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例11.缓释微球的制备。Example 11. Preparation of sustained release microspheres.
将6.50gPLGA(85/15,0.75dl/g,81kDa,羧基端基)溶于150.00g二氯甲烷,得均一溶液A;将3.50g雷沙吉兰溶于10.00g乙酸,得均一溶液B;在2000rpm的涡旋条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入15℃的4.0%的聚乙烯醇连续水相中,使用600bar的高压均质制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。6.50g PLGA (85/15, 0.75dl/g, 81kDa, carboxyl end group) was dissolved in 150.00g of dichloromethane to obtain a homogeneous solution A; 3.50g of rasagiline was dissolved in 10.00g of acetic acid to obtain a uniform solution B; Solution A was added to solution B under vortex conditions of 2000 rpm to obtain a homogeneous emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 4.0% polyvinyl alcohol at 15 ° C, and microspheres were prepared using high pressure homogenization of 600 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例12.缓释微球的制备。Example 12. Preparation of sustained release microspheres.
将6.50gPLGA(100/0,0.3dl/g,27kDa,酯基端基)溶于50.00g二氯甲烷,得均一溶液A;将3.50g雷沙吉兰溶于10.00g乙酸,得均一溶液B;在2000rpm的机械搅拌条件下,将溶液A加入溶液B得均一乳液C。将均一溶液C加入15℃的4.0%的聚乙烯醇连续水相中,使用1500bar的高压均质制备微球。然后升温至40℃使有机溶剂挥发,之后过滤微球,并且使用注射用水清洗微球7次,然后冷冻干燥,得到缓释微球。6.50 g of PLGA (100/0, 0.3 dl/g, 27 kDa, ester end group) was dissolved in 50.00 g of dichloromethane to obtain a homogeneous solution A; 3.50 g of rasagiline was dissolved in 10.00 g of acetic acid to obtain a homogeneous solution B. Solution A was added to solution B under mechanical agitation at 2000 rpm to obtain a uniform emulsion C. The homogeneous solution C was added to a continuous aqueous phase of 4.0% polyvinyl alcohol at 15 ° C, and microspheres were prepared using high pressure homogenization of 1500 bar. Then, the organic solvent was evaporated by heating to 40 ° C, and then the microspheres were filtered, and the microspheres were washed 7 times with water for injection, and then freeze-dried to obtain sustained-release microspheres.
实施例13.微球工艺回收率的测定。Example 13. Determination of microsphere process recovery.
分别取实施例1-12中冻干后得到的缓释微球,称重,然后计算工艺回收率,结果如表1所示。其中,工艺回收率=冻干后微球重量/投料量*100%The sustained-release microspheres obtained after lyophilization in Examples 1-12 were weighed and weighed, and then the process recovery was calculated. The results are shown in Table 1. Among them, the process recovery rate = microsphere weight / feed amount *100% after lyophilization
表1Table 1
项目project 工艺回收率/%Process recovery rate /%
实施例1Example 1 87.587.5
实施例2Example 2 86.786.7
实施例3Example 3 89.389.3
实施例4Example 4 83.283.2
实施例5Example 5 90.590.5
实施例6Example 6 84.284.2
实施例7Example 7 89.589.5
实施例8Example 8 83.983.9
实施例9Example 9 90.390.3
实施例10Example 10 87.687.6
实施例11Example 11 91.591.5
实施例12Example 12 87.787.7
实施例14.缓释微球粒径分布测定。Example 14. Determination of particle size distribution of sustained release microspheres.
采用激光粒度测试仪测定释微球粒径分布。泵速度40%,测定时间90s,等待时间30s,PIDS设置为“开”,测定次数为1。测定时,取缓释微球适量,加入5-10滴1%的表面活性剂溶液,然后再加入1ml水,混匀。打开仪器,向样品池中加样,直至遮光度为8-12%,记录测定结果,平行测定3次,取平均值,结果如表2所示。其中D10表示小于该粒径的微球数量占总量的10%,D50表示中间粒径,即小于该粒径的微球占总量的50%,D90表示小于该粒径的微球数量占总量的90%。The particle size distribution of the microspheres was measured by a laser particle size tester. The pump speed is 40%, the measurement time is 90s, the waiting time is 30s, the PIDS is set to "on", and the number of measurements is 1. For the determination, take appropriate amount of slow-release microspheres, add 5-10 drops of 1% surfactant solution, then add 1ml of water and mix. The instrument was turned on, and the sample was loaded into the sample cell until the opacity was 8-12%. The measurement results were recorded, and the measurements were performed three times in parallel, and the average value was obtained. The results are shown in Table 2. Wherein D10 represents that the number of microspheres smaller than the particle diameter accounts for 10% of the total amount, D50 represents the intermediate particle diameter, that is, the microspheres smaller than the particle diameter account for 50% of the total amount, and D90 represents the number of microspheres smaller than the particle diameter. 90% of the total.
表2Table 2
项目project D10/μmD10/μm D50/μmD50/μm D90/μmD90/μm
实施例1Example 1 38.6438.64 70.2170.21 113.88113.88
实施例2Example 2 0.510.51 0.900.90 2.172.17
实施例3Example 3 29.5329.53 74.0774.07 118.68118.68
实施例4Example 4 0.580.58 1.101.10 1.961.96
实施例5Example 5 35.3435.34 81.0581.05 138.05138.05
实施例6Example 6 0.610.61 2.752.75 4.364.36
实施例7Example 7 27.4627.46 60.5760.57 112.89112.89
实施例8Example 8 0.670.67 2.532.53 3.843.84
实施例9Example 9 23.1723.17 40.3140.31 60.0860.08
实施例10Example 10 0.490.49 0.620.62 1.081.08
实施例11Example 11 65.8965.89 108.4108.4 145.79145.79
实施例12Example 12 3.583.58 4.154.15 4.874.87
实施例15.雷沙吉兰含量测定。Example 15. Determination of rasagiline content.
取缓释微球精密称定,加入乙腈分散微球,然后加入pH值为6.5的三乙氨-冰醋酸缓冲溶液-乙腈(52:48)流动相溶解并定量至约100μg/ml的供试品。同法操作,配制对照品。使用HPLC测定,结果如表3所示。含量为药物量占微球重的百分含量。含量=药物量/微球量*100The slow-release microspheres were accurately weighed, and the acetonitrile-dispersed microspheres were added, and then the mobile phase of the triethylamine-glacial acetic acid buffer solution-acetonitrile (52:48) having a pH of 6.5 was dissolved and quantified to about 100 μg/ml. Product. The same method was used to prepare a reference substance. The results were determined by HPLC, and the results are shown in Table 3. The content is the percentage of the drug amount to the weight of the microspheres. Content = drug amount / microsphere amount * 100
表3table 3
项目project 含量/%content/%
实施例1Example 1 17.517.5
实施例2Example 2 16.916.9
实施例3Example 3 28.728.7
实施例4Example 4 26.826.8
实施例5Example 5 37.437.4
实施例6Example 6 35.935.9
实施例7Example 7 45.645.6
实施例8Example 8 42.342.3
实施例9Example 9 38.738.7
实施例10Example 10 37.937.9
实施例11Example 11 34.734.7
实施例12Example 12 33.933.9
实施例16.缓释微球释放特性。Example 16. Sustained release microsphere release characteristics.
缓释微球的筛分:取实施例1冻干后部分缓释微球,分别用100、115、150、175、230、325、500目筛网筛分,得到不同目数微球,标记为实施例1-1至实施例1-6,如表4所示。用于考察在普通粒径范围内,即20-150μm范围内,不同粒径微球的释放行为差异。下表含义:例如实施例1-1表示将部分实施例1筛分后得到的100-115目的微球。Screening of sustained-release microspheres: Partially-released microspheres were lyophilized in Example 1 and sieved with 100, 115, 150, 175, 230, 325, and 500 mesh screens to obtain different meshes of microspheres. For the examples 1-1 to 1-6, as shown in Table 4. It is used to investigate the difference in release behavior of microspheres with different particle sizes in the range of ordinary particle size, that is, in the range of 20-150 μm. The following table means: For example, Example 1-1 shows a 100-115 mesh microsphere obtained by sieving part of Example 1.
表4Table 4
项目project 目数Number of mesh
实施例1-1Example 1-1 100-115100-115
实施例1-2Example 1-2 115-150115-150
实施例1-3Examples 1-3 150-175150-175
实施例1-4Examples 1-4 175-230175-230
实施例1-5Examples 1-5 230-325230-325
实施例1-6Example 1-6 325-500325-500
分别取实施例1至实施例12制备的缓释微球以及由实施例1筛分成不同粒径的微球即实施例1-2、实施例1-4、实施例1-6进行体外释放。The sustained-release microspheres prepared in Examples 1 to 12 and the microspheres sieved into different particle diameters in Example 1, that is, Example 1-2, Example 1-4, and Example 1-6, were released in vitro.
测试方法:精密称定微球(30mg),加入100ml的pH值为7.4的PBS作为释放介质,于37℃水浴摇床中进行释放实验。摇床转速100rpm,在固定的时间,取出样品静置,然后 取上清液并过0.45μm微孔滤膜,同时补充新鲜的释放介质,使用HPLC测定含量。每批次微球平行三份进行。释放数据如下表5、表6以及图1至图7所示。Test method: Microspheres (30 mg) were accurately weighed, and 100 ml of PBS having a pH of 7.4 was added as a release medium, and a release experiment was carried out in a 37 ° C water bath shaker. The shaker was rotated at 100 rpm. At a fixed time, the sample was taken out and allowed to stand, and then the supernatant was passed through a 0.45 μm microporous membrane while fresh release medium was added and the content was determined by HPLC. Each batch of microspheres was run in triplicate. The release data is shown in Table 5, Table 6, and Figures 1 to 7 below.
通过实施例1-1、实施例1-4、实施例1-6释放结果可知,在普通粒径范围内,即20-150μm粒径范围内,虽然不同粒径范围微球释放行为有差异,但是并不明显。According to the results of the release of Examples 1-1, 1-4 and 1-6, in the range of the ordinary particle size, that is, in the range of 20-150 μm, although the release behavior of the microspheres in different particle size ranges is different, But it is not obvious.
通过实施例1、实施例3、实施例5、实施例7、实施例9、实施例11释放行为可知,在普通粒径范围内,即20-150μm之间,微球释放期较长,但出现了延迟释放期;通过实施例2、实施例4、实施例6、实施例8、实施例10、实施例12释放数据可知,在纳米至亚微米粒径范围内,即0.5-5微米之间,微球释放期较短,但无延迟释放期且无突释。According to the release behaviors of Example 1, Example 3, Example 5, Example 7, Example 9, and Example 11, it can be seen that the microsphere release period is longer in the range of the ordinary particle size, that is, between 20 and 150 μm. A delayed release period occurs; by the release data of Example 2, Example 4, Example 6, Example 8, Example 10, and Example 12, it is known that the nanometer to submicron particle size range, that is, 0.5-5 micrometers During the period, the release period of the microspheres was short, but there was no delayed release period and no burst release.
而通过将纳米至亚微米粒径微球与普通粒径微球按照一定的比例混合,如实施例1释放周期为30天,延迟释放期为10天,而实施例2释放周期为10天,无延迟释放期。那么可以将实施例1与实施例2组合使用。刚好实施例2微球负责组合药物的前期释放,实施例1微球负责后期释放。若整个释放周期需要的药物剂量为3份,则实施例1提供两份,实施例2提供一份。具体的若整个释放周期需要的药物剂量为30mg,则实施例1需要提供20mg药物,即72.73mg微球(微球重量=所需药物量/含量);实施例2需要提供10mg药物,即37.17mg微球;以此类推三份实施例3与一份实施例4混合(释放周期5.7周左右)、三份实施例5与一份实施例6混合(释放周期8.6周左右)、两份实施例7与一份实施例8混合(释放周期12周左右)、五份实施例9与一份实施例8混合(释放周期6周左右)、三份实施例11与两份实施例12混合(释放周期7周左右),然后进行体外释放实验,即可以得到释放周期4-12周,且无突释和延迟释放期的药物组合物。混合的前提是纳米到亚微米微球的释放期能与普通粒径微球的延迟释放期刚好重叠。实施例2/4/6/8/10/12分别对应的是实施例1/3/5/7/9/11的纳米到亚微米粒径微球,两者混合可以达到较长释放期并无延迟释放期的目的。By mixing the nano-submicron particle size microspheres with the ordinary particle size microspheres in a certain ratio, as in the case of the release period of the first embodiment, the release period is 30 days, and the release period of the embodiment 2 is 10 days. No delayed release period. Then, Example 1 can be used in combination with Example 2. The microspheres of Example 2 were responsible for the prophase release of the combination drug, and the microspheres of Example 1 were responsible for the later release. If the drug dosage required for the entire release cycle is 3 parts, then Example 1 provides two copies and Example 2 provides one portion. Specifically, if the drug dosage required for the entire release cycle is 30 mg, then Example 1 needs to provide 20 mg of the drug, that is, 72.73 mg of microspheres (microsphere weight = required drug amount/content); Example 2 requires 10 mg of drug, ie 37.17 Mg microspheres; such as three parts of Example 3 mixed with one part of Example 4 (release cycle of about 5.7 weeks), three parts of Example 5 mixed with one part of Example 6 (release cycle of about 8.6 weeks), two implementations Example 7 was mixed with one part of Example 8 (release cycle of about 12 weeks), five parts of Example 9 were mixed with one part of Example 8 (release cycle of about 6 weeks), and three parts of Example 11 were mixed with two parts of Example 12 ( The release period is about 7 weeks), and then an in vitro release test is performed, that is, a pharmaceutical composition having a release period of 4 to 12 weeks and no burst release and delayed release period can be obtained. The premise of mixing is that the release period of the nano-submicron microspheres can just overlap with the delayed release period of the ordinary particle size microspheres. Examples 2/4/6/8/10/12 correspond to the nano-to-submicron particle size microspheres of Example 1/3/5/7/9/11, respectively, which can achieve a longer release period and No purpose for a delayed release period.
表5table 5
Figure PCTCN2018089384-appb-000001
Figure PCTCN2018089384-appb-000001
Figure PCTCN2018089384-appb-000002
Figure PCTCN2018089384-appb-000002
表6Table 6
Figure PCTCN2018089384-appb-000003
Figure PCTCN2018089384-appb-000003
Figure PCTCN2018089384-appb-000004
Figure PCTCN2018089384-appb-000004
Figure PCTCN2018089384-appb-000005
Figure PCTCN2018089384-appb-000005
Figure PCTCN2018089384-appb-000006
Figure PCTCN2018089384-appb-000006
Figure PCTCN2018089384-appb-000007
Figure PCTCN2018089384-appb-000007
综上所述,本研究发现在微球常规粒径范围内,随着微球粒径的减小,微球释放周期以及延迟释放期确实会变短,但是变化均不明显。另外创造性的发现,将微球制备成亚微米级别,微球释放行为却发生了明显的改变,第一是无延迟释放期且无突释,第二是释放周期明显缩短。同时意外地发现本发明的亚微米级别微球的释放期与普通粒径微球的延迟释放期相同。通过将两种不同粒径的微球混合使用,不仅得到释放周期较长的产品,且无延迟释放期。且利用本技术方案可以得到高载药量和高包封率的微球,通过在本发明的药物组合物中使用2种不同粒径微球的适宜组合,可以显著减少血浆中雷沙吉兰浓度的波动,且无明显的延迟释放期。同时,本发明在载药量高的情况下,药物无突释。In summary, this study found that within the conventional particle size range of the microspheres, as the particle size of the microspheres decreases, the microsphere release cycle and the delayed release period do become shorter, but the changes are not obvious. In addition, the creative discovery found that the microspheres were prepared to a submicron level, and the microsphere release behavior changed significantly. The first was no delayed release period and no burst release, and the second was that the release cycle was significantly shortened. At the same time, it was unexpectedly found that the release period of the submicron-sized microspheres of the present invention is the same as that of the ordinary particle size microspheres. By mixing two microspheres of different particle sizes, not only a product with a long release period but also a delayed release period is obtained. The microspheres with high drug loading and high encapsulation efficiency can be obtained by using the technical scheme, and the rasagiline in plasma can be significantly reduced by using a suitable combination of two microspheres of different particle sizes in the pharmaceutical composition of the invention. Fluctuations in concentration without significant delayed release. At the same time, in the case of high drug loading, the present invention has no sudden release of the drug.

Claims (11)

  1. 一种治疗帕金森病药物的长效缓释制剂,其特征在于,所述长效缓释制剂为微球,所述微球包含雷沙吉兰或其药物学可接受的盐和生物可降解生物相容性高分子聚合物,所述微球包括平均粒径为0.5-5μm的微球和平均粒径为20-150μm的微球。A long-acting sustained-release preparation for treating a Parkinson's disease drug, characterized in that the long-acting sustained-release preparation is a microsphere comprising rasagiline or a pharmaceutically acceptable salt thereof and biodegradable A biocompatible high molecular polymer comprising microspheres having an average particle diameter of 0.5 to 5 μm and microspheres having an average particle diameter of 20 to 150 μm.
  2. 根据权利要求1所述的长效缓释制剂,其特征在于,所述平均粒径为0.5-5μm的微球占长效缓释制剂的10-50wt%,平均粒径为20-150μm的微球占50-90wt%。The long-acting sustained-release preparation according to claim 1, wherein the microspheres having an average particle diameter of 0.5 to 5 μm account for 10 to 50% by weight of the long-acting sustained-release preparation, and the average particle diameter is 20 to 150 μm. The ball accounts for 50-90% by weight.
  3. 根据权利要求1所述的长效缓释制剂,其特征在于,雷沙吉兰或其药学上可接受的盐占长效缓释制剂的10-50wt%。The long-acting sustained-release preparation according to claim 1, wherein rasagiline or a pharmaceutically acceptable salt thereof accounts for 10 to 50% by weight of the long-acting sustained-release preparation.
  4. 根据权利要求1所述的长效缓释制剂,其特征在于,所述生物可降解生物相容性高分子聚合物为聚(丙交酯-乙交酯)。The long-acting sustained release preparation according to claim 1, wherein the biodegradable biocompatible high molecular polymer is poly(lactide-glycolide).
  5. 根据权利要求4所述的长效缓释制剂,其特征在于,所述聚(丙交酯-乙交酯)中,丙交酯和乙交酯的摩尔比为65:35~100:0。The long-acting sustained-release preparation according to claim 4, wherein a molar ratio of lactide to glycolide in the poly(lactide-glycolide) is from 65:35 to 100:0.
  6. 根据权利要求4所述的长效缓释制剂,其特征在于,所述聚(丙交酯-乙交酯)的粘度范围为0.2-0.8dl/g。The long-acting sustained-release preparation according to claim 4, wherein the poly(lactide-glycolide) has a viscosity in the range of 0.2 to 0.8 dl/g.
  7. 根据权利要求4所述的长效缓释制剂,其特征在于,所述聚(丙交酯-乙交酯)的分子量范围21kDa-89kDa。The long-acting sustained-release preparation according to claim 4, wherein the poly(lactide-glycolide) has a molecular weight ranging from 21 kDa to 89 kDa.
  8. 根据权利要求1所述的长效缓释制剂,其特征在于,所述长效缓释制剂的释放周期在4~12周。The long-acting sustained-release preparation according to claim 1, wherein the long-acting sustained-release preparation has a release period of 4 to 12 weeks.
  9. 一种治疗帕金森病药物的长效缓释制剂的制备方法,其特征在于,包括如下步骤:A preparation method of a long-acting sustained-release preparation for treating a Parkinson's disease medicine, comprising the following steps:
    a)将生物可降解生物相容性高分子溶于第一类有机溶剂,得到均一溶液A;a) dissolving the biodegradable biocompatible polymer in the first type of organic solvent to obtain a uniform solution A;
    b)将雷沙吉兰或其药物学可接受的盐溶于能与第一类有机溶剂互溶的第二类有机溶剂,得均一溶液B;b) rasagiline or a pharmaceutically acceptable salt thereof is dissolved in a second type of organic solvent which is miscible with the first type of organic solvent to obtain a homogeneous solution B;
    c)将步骤b)得到的均一溶液B加入步骤a)得到的均一溶液A中得到均一乳液C;c) the uniform solution B obtained in step b) is added to the homogeneous solution A obtained in step a) to obtain a uniform emulsion C;
    d)将步骤c)得到的均一乳液C加入用药用水溶性高分子配制的连续水相溶液中以形成微球;d) adding the uniform emulsion C obtained in the step c) to a continuous aqueous phase solution prepared by using a pharmaceutically acceptable water-soluble polymer to form microspheres;
    e)去除步骤d)微球中的有机溶剂,过滤,洗涤;e) removing the organic solvent in the step d) microspheres, filtering, washing;
    f)将步骤e)所得微球冷冻干燥,得到缓释微球。f) The microspheres obtained in step e) are freeze-dried to obtain sustained-release microspheres.
  10. 根据权利要求8所述的制备方法,其特征在于,第一类有机溶剂选自二氯甲烷、乙酸乙酯、四氢呋喃、二甲基亚砜、二甲基甲酰胺或二甲基乙酰胺中的任意一种;第二类有机溶剂选自乙醇、乙酸、盐酸、二甲基亚砜、二甲基甲酰胺或二甲基乙酰胺中的任意一种。The preparation method according to claim 8, wherein the first type of organic solvent is selected from the group consisting of dichloromethane, ethyl acetate, tetrahydrofuran, dimethyl sulfoxide, dimethylformamide or dimethylacetamide. Any one; the second type of organic solvent is selected from any one of ethanol, acetic acid, hydrochloric acid, dimethyl sulfoxide, dimethylformamide or dimethylacetamide.
  11. 根据权利要求9-10任一项所述的制备方法,其特征在于,第一类有机溶剂与第二类有机溶剂的比例为2:1-20:1.。The preparation method according to any one of claims 9 to 10, wherein the ratio of the first type of organic solvent to the second type of organic solvent is from 2:1 to 20:1.
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