CN116444516A - Paliperidone palmitate nanocrystals and preparation method thereof, paliperidone palmitate nanocrystal suspension injection and preparation method thereof - Google Patents
Paliperidone palmitate nanocrystals and preparation method thereof, paliperidone palmitate nanocrystal suspension injection and preparation method thereof Download PDFInfo
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- CN116444516A CN116444516A CN202310279892.2A CN202310279892A CN116444516A CN 116444516 A CN116444516 A CN 116444516A CN 202310279892 A CN202310279892 A CN 202310279892A CN 116444516 A CN116444516 A CN 116444516A
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- VOMKSBFLAZZBOW-UHFFFAOYSA-N 3-{2-[4-(6-fluoro-1,2-benzoxazol-3-yl)piperidin-1-yl]ethyl}-2-methyl-4-oxo-6,7,8,9-tetrahydropyrido[1,2-a]pyrimidin-9-yl hexadecanoate Chemical compound FC1=CC=C2C(C3CCN(CC3)CCC3=C(C)N=C4N(C3=O)CCCC4OC(=O)CCCCCCCCCCCCCCC)=NOC2=C1 VOMKSBFLAZZBOW-UHFFFAOYSA-N 0.000 title claims abstract description 147
- 229960000635 paliperidone palmitate Drugs 0.000 title claims abstract description 147
- 239000002159 nanocrystal Substances 0.000 title claims abstract description 61
- 239000000725 suspension Substances 0.000 title claims abstract description 33
- 238000002347 injection Methods 0.000 title claims abstract description 27
- 239000007924 injection Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 108
- 238000002425 crystallisation Methods 0.000 claims abstract description 83
- 230000008025 crystallization Effects 0.000 claims abstract description 80
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 54
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 54
- 239000002245 particle Substances 0.000 claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 20
- 239000003960 organic solvent Substances 0.000 claims abstract description 14
- 230000008569 process Effects 0.000 claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 61
- 239000000243 solution Substances 0.000 claims description 52
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 36
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 33
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 16
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 12
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000009826 distribution Methods 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 11
- 239000011259 mixed solution Substances 0.000 claims description 11
- 239000008215 water for injection Substances 0.000 claims description 11
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 claims description 10
- 238000005507 spraying Methods 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 8
- 239000003814 drug Substances 0.000 abstract description 12
- 239000002904 solvent Substances 0.000 abstract description 11
- 230000002776 aggregation Effects 0.000 abstract description 9
- 229940079593 drug Drugs 0.000 abstract description 9
- 238000005054 agglomeration Methods 0.000 abstract description 7
- 238000001035 drying Methods 0.000 abstract description 7
- 239000013078 crystal Substances 0.000 abstract description 4
- 238000004220 aggregation Methods 0.000 abstract description 3
- 239000003381 stabilizer Substances 0.000 abstract description 3
- 238000009825 accumulation Methods 0.000 abstract description 2
- 238000002309 gasification Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 description 8
- 238000005070 sampling Methods 0.000 description 7
- 238000004817 gas chromatography Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- PMXMIIMHBWHSKN-UHFFFAOYSA-N 3-{2-[4-(6-fluoro-1,2-benzoxazol-3-yl)piperidin-1-yl]ethyl}-9-hydroxy-2-methyl-6,7,8,9-tetrahydropyrido[1,2-a]pyrimidin-4-one Chemical compound FC1=CC=C2C(C3CCN(CC3)CCC=3C(=O)N4CCCC(O)C4=NC=3C)=NOC2=C1 PMXMIIMHBWHSKN-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 3
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 3
- 239000002671 adjuvant Substances 0.000 description 3
- 239000011324 bead Substances 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 229960001057 paliperidone Drugs 0.000 description 3
- 229910052726 zirconium Inorganic materials 0.000 description 3
- 238000000498 ball milling Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000009924 canning Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 1
- 206010059866 Drug resistance Diseases 0.000 description 1
- 241000219099 Parthenocissus quinquefolia Species 0.000 description 1
- 235000009388 Parthenocissus quinquefolia Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000000561 anti-psychotic effect Effects 0.000 description 1
- 239000012296 anti-solvent Substances 0.000 description 1
- 239000000164 antipsychotic agent Substances 0.000 description 1
- 229940005529 antipsychotics Drugs 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 208000000509 infertility Diseases 0.000 description 1
- 230000036512 infertility Effects 0.000 description 1
- 208000021267 infertility disease Diseases 0.000 description 1
- 238000010255 intramuscular injection Methods 0.000 description 1
- 239000007927 intramuscular injection Substances 0.000 description 1
- 210000003734 kidney Anatomy 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 208000030159 metabolic disease Diseases 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 229960005017 olanzapine Drugs 0.000 description 1
- KVWDHTXUZHCGIO-UHFFFAOYSA-N olanzapine Chemical compound C1CN(C)CCN1C1=NC2=CC=CC=C2NC2=C1C=C(C)S2 KVWDHTXUZHCGIO-UHFFFAOYSA-N 0.000 description 1
- 201000000980 schizophrenia Diseases 0.000 description 1
- 238000001238 wet grinding Methods 0.000 description 1
Classifications
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/0012—Galenical forms characterised by the site of application
- A61K9/0019—Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/02—Inorganic compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/06—Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite
- A61K47/08—Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite containing oxygen, e.g. ethers, acetals, ketones, quinones, aldehydes, peroxides
- A61K47/12—Carboxylic acids; Salts or anhydrides thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/30—Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
- A61K47/32—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. carbomers, poly(meth)acrylates, or polyvinyl pyrrolidone
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/10—Dispersions; Emulsions
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P25/00—Drugs for disorders of the nervous system
- A61P25/18—Antipsychotics, i.e. neuroleptics; Drugs for mania or schizophrenia
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D471/00—Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, at least one ring being a six-membered ring with one nitrogen atom, not provided for by groups C07D451/00 - C07D463/00
- C07D471/02—Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, at least one ring being a six-membered ring with one nitrogen atom, not provided for by groups C07D451/00 - C07D463/00 in which the condensed system contains two hetero rings
- C07D471/04—Ortho-condensed systems
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
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- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Epidemiology (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Dermatology (AREA)
- Dispersion Chemistry (AREA)
- Psychiatry (AREA)
- Biomedical Technology (AREA)
- Neurology (AREA)
- Neurosurgery (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Nitrogen Condensed Heterocyclic Rings (AREA)
Abstract
The invention provides paliperidone palmitate nanocrystals, a preparation method thereof, paliperidone palmitate nanocrystal suspension injection and a preparation method thereof, and relates to the technical field of drug production. According to the invention, the paliperidone palmitate is dissolved in the organic solvent and then subjected to carbon dioxide supercritical crystallization, the obtained paliperidone palmitate nanocrystals reach nanoscale, the separation speed of the crystals and the organic solvent is high in the crystallization process, a large amount of energy is taken away in the carbon dioxide gasification process, the prepared nanocrystals have no charge accumulation, the surface free energy is low, agglomeration and aggregation among particles are difficult, no stabilizer is required to be additionally added after the paliperidone palmitate nanocrystal suspension injection is prepared, and the production cost of the paliperidone palmitate nanocrystal suspension injection is reduced. In addition, the organic solvent is taken away by carbon dioxide in the crystallization process, no solvent residue exists, and further drying treatment is not needed, so that the problem of solvent residue in the traditional solvent crystallization method is solved, and the phenomenon of agglomeration of paliperidone palmitate nanocrystals in the drying process is avoided.
Description
Technical Field
The invention relates to the technical field of medicine production, in particular to paliperidone palmitate nanocrystals, a preparation method thereof, paliperidone palmitate nanocrystal suspension injection and a preparation method thereof.
Background
Paliperidone palmitate is a second generation novel antipsychotic developed by the Qiangsheng company, can effectively overcome the time lag barrier of other long-acting antipsychotics, and can be used for treating the acute phase and the maintenance phase of schizophrenia at the same time. In addition, paliperidone does not cause the extensive metabolism of liver, and is secreted in a large amount through the kidney without change, and is superior to the olanzapine which is a traditional medicine in the aspects of safety, drug resistance and the like, and meanwhile, metabolic disorder is less, so that the paliperidone has good application prospect.
The paliperidone palmitate is prepared into fine particles, the surface area of the particles is increased, the water solubility is improved, an aqueous suspension preparation suitable for intramuscular injection administration is formed, and the absorption rate and the bioavailability of the medicine are also improved. Two paliperidone palmitate nanocrystalline suspension products are marketed by the western ampelopsis pharmaceutical company in 2009 and 2015, and both products adopt nanocrystalline preparation technology. At present, the preparation technology of paliperidone palmitate nanocrystalline mainly adopts a grinding method and a solvent method.
For example, chinese patents CN106137985A, CN1093762a and CN1160074a disclose that the particle size of paliperidone palmitate is reduced to nano-scale by wet ball milling, thereby increasing the specific surface area and bioavailability of paliperidone palmitate. However, the use of ball milling to prepare the paliperidone palmitate nanocrystalline suspension requires the reliance on ball mill equipment, and the process involves replacement of the milled zirconium beads under aseptic conditions, not only increasing the risk of sterility challenges, but also the use of milled zirconium beads presents a risk of media residue. In addition, the milling process results in a significant increase in the surface energy of the drug particles, and a challenge is how to select appropriate adjuvants/stabilizers to avoid re-agglomeration of the drug particles into a wet milling dispersion process that can successfully obtain nanocrystals.
Compared with the grinding method, the solvent method has the advantages of no special requirements on equipment, low cost and no residues of the grinding zirconium beads. For example, chinese patent CN109400602a discloses the preparation of smaller size drug particles by anti-solvent precipitation, taking advantage of the difference in solubility of paliperidone palmitate in dichloromethane and n-heptane. Foreign patent WO2016199170 discloses that the dissolution of paliperidone palmitate in hot ethanol, and the momentary precipitation of paliperidone palmitate by rapid cooling, makes it possible to obtain nano-sized drug particles. However, the above solvent crystallization methods all use an organic solvent, and require further drying to remove the solvent residue. The drying process inevitably leads to aggregation and agglomeration of the drug particles, and the drug suspension with nano-scale and uniform dispersion cannot be prepared; moreover, the agglomeration of the drug particles during the drying process easily results in the inability of the organic solvents to be removed effectively, and the risk of drug safety is extremely high.
Disclosure of Invention
In view of the above, the invention aims to provide paliperidone palmitate nanocrystals and a preparation method thereof, paliperidone palmitate nanocrystal suspension injection and a preparation method thereof, and the paliperidone palmitate nanocrystals prepared by the invention have no solvent residue and crystal grains do not agglomerate.
In order to achieve the above object, the present invention provides the following technical solutions:
the invention provides a preparation method of paliperidone palmitate nanocrystals, which comprises the following steps:
and dissolving paliperidone palmitate in an organic solvent, and performing carbon dioxide supercritical crystallization on the paliperidone palmitate solution to obtain paliperidone palmitate nanocrystals.
Preferably, the concentration of the paliperidone palmitate solution is 10-100 g/mL;
the organic solvent comprises one or more of methanol, ethanol and acetone.
Preferably, the supercritical crystallization of carbon dioxide comprises:
introducing carbon dioxide into a crystallization kettle, spraying paliperidone palmitate solution into the crystallization kettle through a nozzle positioned at the top of the crystallization kettle, and performing supercritical carbon dioxide crystallization.
Preferably, the temperature of the crystallization kettle is 35-55 ℃ and the pressure is 10-30 MPa.
Preferably, the temperature of the nozzle is 40-45 ℃.
Preferably, after the paliperidone palmitate solution is stopped from being sprayed, the carbon dioxide is continuously introduced for 30-60 min.
Preferably, the flow rate ratio of the paliperidone palmitate solution to the carbon dioxide is 15-60: 1.
the invention provides paliperidone palmitate nanocrystals prepared by the preparation method in the technical scheme, and the particle size distribution range is as follows: d (D) 10 Is 0.3-0.6 mu m, D 50 Is 0.9-1.4 mu m, D 90 2.0-4.4 μm.
The invention provides paliperidone palmitate nanocrystalline suspension injection, which comprises the following components in parts by mass: 100 parts of paliperidone palmitate nanocrystals, 2.5-3.5 parts of citric acid, 2.5-3.5 parts of disodium hydrogen phosphate, 1.4-1.9 parts of sodium hydroxide, 15-21 parts of polyvinyl alcohol and 1000-1100 parts of water for injection.
The invention also provides a preparation method of the paliperidone palmitate nanocrystalline suspension injection, which comprises the following steps:
mixing citric acid, disodium hydrogen phosphate, sodium hydroxide, polyvinyl alcohol and water for injection to obtain an auxiliary material mixed solution;
and mixing the auxiliary material mixed solution with paliperidone palmitate nanocrystals to obtain paliperidone palmitate nanocrystal suspension injection.
The invention provides a preparation method of paliperidone palmitate nanocrystals, which comprises the following steps: and dissolving paliperidone palmitate in an organic solvent, and performing carbon dioxide supercritical crystallization on the paliperidone palmitate solution to obtain paliperidone palmitate nanocrystals. The invention adopts a carbon dioxide supercritical crystallization mode to prepare the nano paliperidone palmitate crystals, the separation speed of the crystals and the organic solvent is high in the carbon dioxide supercritical crystallization process, a large amount of energy is taken away in the carbon dioxide gasification process, the prepared nanocrystals have no charge accumulation, the free energy of the surfaces is lower, agglomeration and aggregation among the nanocrystal particles are difficult, and the paliperidone palmitate nanocrystals prepared by the invention are used for preparing suspension without adding a stabilizer, so that the production cost of paliperidone palmitate nanocrystal suspension injection is reduced. In addition, the organic solvent is taken away by carbon dioxide in the crystallization process, no solvent residue exists, and further drying treatment is not needed, so that the problem of solvent residue in the traditional solvent crystallization method is solved, and the phenomenon of agglomeration of paliperidone palmitate nanocrystals in the drying process is avoided.
Detailed Description
The invention provides a preparation method of paliperidone palmitate nanocrystals, which comprises the following steps:
and dissolving paliperidone palmitate in an organic solvent, and performing carbon dioxide supercritical crystallization on the paliperidone palmitate solution to obtain paliperidone palmitate nanocrystals.
The raw materials adopted by the invention are all commercial products unless specified.
In the present invention, the organic solvent preferably includes one or more of methanol, ethanol and acetone, more preferably methanol, ethanol or acetone. In the present invention, the concentration of the paliperidone palmitate solution is preferably 10 to 100g/mL, more preferably 20 to 80g/mL, and even more preferably 40 to 60g/mL.
In the present invention, the supercritical carbon dioxide crystallization specifically includes: introducing carbon dioxide into a crystallization kettle, spraying paliperidone palmitate solution into the crystallization kettle through a nozzle positioned at the top of the crystallization kettle, and performing supercritical carbon dioxide crystallization.
In the present invention, the flow rate of the carbon dioxide is preferably 1 to 2L/min, more preferably 1.2 to 1.8L/min, and still more preferably 1.4 to 1.5L/min; according to the invention, before the paliperidone palmitate solution is sprayed, the carbon dioxide is introduced for a period of time not limited, so that the pressure of the crystallization kettle is kept between 10 and 30MPa, and the pressure of the crystallization kettle is more preferably between 15 and 25MPa, and further preferably 20MPa; the temperature of the crystallization vessel is preferably 35 to 55 ℃, more preferably 40 to 50 ℃, and even more preferably 40 ℃.
In the present invention, the temperature of the nozzle is preferably 40 to 45 ℃, more preferably 41 to 44 ℃, and even more preferably 42 to 43 ℃. In the present invention, the flow rate ratio of paliperidone palmitate solution to carbon dioxide is preferably 15 to 60:1, more preferably 20 to 50:1, more preferably 30 to 40:1. in the present invention, the flow rate of the paliperidone palmitate solution is preferably 30 to 60mL/min, more preferably 35 to 55mL/min, and even more preferably 40 to 50mL/min. In the present invention, the continuous carbon dioxide supply time after the paliperidone palmitate solution is stopped from being sprayed is preferably 30 to 60 minutes, more preferably 35 to 55 minutes, and even more preferably 40 to 50 minutes.
The supercritical crystallization of the carbon dioxide is completed, and the invention preferably further comprises stopping introducing the carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, and collecting paliperidone palmitate nanocrystals.
The invention provides paliperidone palmitate nanocrystals prepared by the preparation method, wherein the particle size distribution range of the paliperidone palmitate nanocrystals is as follows: d (D) 10 Is 0.3-0.6 mu m, D 50 Is 0.9-1.4 mu m, D 90 2.0-4.4 μm. In the present invention, the paliperidone palmitate nanocrystals D 10 Preferably 0.4 to 0.5 μm, D 50 Preferably 1 to 1.2 μm, D 90 Preferably 3 to 4. Mu.m.
The invention provides paliperidone palmitate nanocrystalline suspension injection, which comprises the following components in parts by mass: 100 parts of paliperidone palmitate nanocrystals, 2.5-3.5 parts of citric acid, 2.5-3.5 parts of disodium hydrogen phosphate, 1.4-1.9 parts of sodium hydroxide, 15-21 parts of polyvinyl alcohol and 1000-1100 parts of water for injection.
The paliperidone palmitate nanocrystalline suspension injection provided by the invention comprises 100 parts of paliperidone palmitate nanocrystalline according to the technical scheme.
The paliperidone palmitate nanocrystalline suspension injection provided by the invention comprises 2.5-3.5 parts of citric acid, preferably 2.8-3.2 parts of citric acid, and more preferably 3 parts of citric acid.
The paliperidone palmitate nanocrystalline suspension injection provided by the invention comprises 2.5-3.5 parts by weight of disodium hydrogen phosphate, preferably 2.8-3.2 parts by weight of paliperidone palmitate nanocrystalline, and more preferably 3 parts by weight of paliperidone palmitate nanocrystalline suspension injection.
The paliperidone palmitate nanocrystalline suspension injection provided by the invention comprises 1.4-1.9 parts of sodium hydroxide, preferably 1.5-1.8 parts of sodium hydroxide, and more preferably 1.6-1.7 parts of paliperidone palmitate nanocrystalline.
The paliperidone palmitate nanocrystalline suspension injection provided by the invention comprises 15-21 parts of polyvinyl alcohol, preferably 16-20 parts, more preferably 17-19 parts, and even more preferably 18 parts by mass of paliperidone palmitate nanocrystalline. In the present invention, the polyvinyl alcohol is preferably polyvinyl alcohol 4000.
The paliperidone palmitate nanocrystalline suspension injection provided by the invention comprises 1000-1100 parts of water for injection, preferably 1020-1080 parts, more preferably 1040-1060 parts, and even more preferably 1050 parts, based on the mass parts of paliperidone palmitate nanocrystals.
The invention also provides a preparation method of the paliperidone palmitate nanocrystalline suspension injection, which comprises the following steps:
mixing citric acid, disodium hydrogen phosphate, sodium hydroxide, polyvinyl alcohol and water for injection to obtain an auxiliary material mixed solution;
and mixing the auxiliary material mixed solution with paliperidone palmitate nanocrystals to obtain paliperidone palmitate nanocrystal suspension injection.
The invention mixes citric acid, disodium hydrogen phosphate, sodium hydroxide, polyvinyl alcohol and water for injection to obtain auxiliary material mixed solution. The mode of the mixing is not particularly limited in the present invention, and the raw materials may be dissolved in water for injection, and specifically, the raw materials may be mixed by stirring.
After the auxiliary material mixed solution is obtained, the auxiliary material mixed solution is mixed with paliperidone palmitate nanocrystals to obtain paliperidone palmitate nanocrystal suspension injection. The mode of the mixing is not particularly limited in the present invention, and the raw materials may be uniformly mixed, and in particular, the raw materials may be mixed by stirring.
The technical solutions of the present invention will be clearly and completely described in the following in connection with the embodiments of the present invention. It will be apparent that the described embodiments are only some, but not all, embodiments of the invention. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Example 1
Paliperidone palmitate 10g was dissolved in 1000mL of methanol to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 35 ℃ and the temperature of a nozzle to be 40 ℃; introducing carbon dioxide at a flow rate of 1L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 15MPa. Opening a high-pressure metering pump, setting the sampling rate of the paliperidone palmitate methanol solution to be 30mL/min, spraying the paliperidone palmitate solution into the crystallization kettle through a nozzle at the top of the crystallization kettle by the high-pressure metering pump, and after the paliperidone palmitate methanol solution is completely added, closing the high-pressure metering pump, and continuously introducing carbon dioxide for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, collecting and obtaining 8.5g of white paliperidone palmitate nanocrystals, and detecting the granularity distribution of the nanocrystals by a Markov laser granularity meter to be: d (D) 10 0.3μm,D 50 0.9μm,D 90 2.0 μm. The methanol was not detected by gas chromatography.
Example 2
Paliperidone palmitate 10g was dissolved in 100mL of methanol to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 35 ℃ and the temperature of a nozzle to be 40 ℃; introducing carbon dioxide at a flow rate of 1L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 15MPa. Opening a high-pressure metering pump, and setting the methanol solution of paliperidone palmitateAnd the sample rate is 30mL/min, the paliperidone palmitate solution is sprayed into the crystallization kettle through a nozzle at the top of the crystallization kettle by a high-pressure metering pump, and after the paliperidone palmitate methanol solution is completely added, the high-pressure metering pump is closed, and carbon dioxide is continuously introduced for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, collecting and obtaining 8.0g of white paliperidone palmitate nanocrystals, and detecting the particle size distribution by a Markov laser particle sizer: d (D) 10 0.6μm,D 50 1.4μm,D 90 4.4 μm. The methanol was not detected by gas chromatography.
Example 3
Paliperidone palmitate 10g was dissolved in 1000mL of methanol to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 55 ℃ and setting the temperature of a nozzle to be 55 ℃; introducing carbon dioxide at a flow rate of 2L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 30MPa. Opening a high-pressure metering pump, setting the sampling rate of the paliperidone palmitate methanol solution to be 30mL/min, spraying the paliperidone palmitate solution into the crystallization kettle through a nozzle at the top of the crystallization kettle by the high-pressure metering pump, and after the paliperidone palmitate methanol solution is completely added, closing the high-pressure metering pump, and continuously introducing carbon dioxide for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, collecting and obtaining 8.8g of white paliperidone palmitate nanocrystals, and detecting the particle size distribution by a Markov laser particle sizer: d (D) 10 0.5μm,D 50 1.0μm,D 90 3.5 μm. The methanol was not detected by gas chromatography.
Example 4
Paliperidone palmitate 10g was dissolved in 500mL methanol to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 45 ℃ and setting the temperature of a nozzle to be 45 ℃; introducing carbon dioxide at a flow rate of 2L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 20MPa. Opening a high-pressure metering pump, setting the sampling rate of the paliperidone palmitate methanol solution to be 60mL/min, spraying the paliperidone palmitate solution into the crystallization kettle through a nozzle at the top of the crystallization kettle by the high-pressure metering pump, and after the paliperidone palmitate methanol solution is completely addedThe high-pressure metering pump is closed, and carbon dioxide is continuously introduced for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, collecting and obtaining 8.6g of white paliperidone palmitate nanocrystals, and detecting the particle size distribution by a Markov laser particle sizer: d (D) 10 0.4μm,D 50 1.1μm,D 90 3.0 μm. The methanol was not detected by gas chromatography.
Example 5
Paliperidone palmitate 10g was dissolved in 500mL acetone to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 45 ℃ and setting the temperature of a nozzle to be 45 ℃; introducing carbon dioxide at a flow rate of 2L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 20MPa. Opening a high-pressure metering pump, setting the sampling rate of the paliperidone palmitate methanol solution to be 60mL/min, spraying the paliperidone palmitate solution into the crystallization kettle through a nozzle at the top of the crystallization kettle by the high-pressure metering pump, and after the paliperidone palmitate acetone solution is completely added, closing the high-pressure metering pump, and continuously introducing carbon dioxide for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, collecting and obtaining 8.7g of white paliperidone palmitate nanocrystals, and detecting the particle size distribution by a Markov laser particle sizer: d (D) 10 0.4μm,D 50 1.2μm,D 90 3.4 μm. The acetone was not detected by gas chromatography.
Example 6
Paliperidone palmitate 10g was dissolved in 500mL acetone to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 35 ℃ and the temperature of a nozzle to be 40 ℃; introducing carbon dioxide at a flow rate of 2L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 10MPa. Opening a high-pressure metering pump, setting the sampling rate of the paliperidone palmitate methanol solution to be 30mL/min, spraying the paliperidone palmitate solution into the crystallization kettle through a nozzle at the top of the crystallization kettle by the high-pressure metering pump, and after the paliperidone palmitate acetone solution is completely added, closing the high-pressure metering pump, and continuously introducing carbon dioxide for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, and collecting 8.8g of white paliperidine palmitateThe particle size distribution of the methylphenol nanocrystals was measured by a malvern laser particle sizer: d (D) 10 0.3μm,D 50 1.0μm,D 90 2.5 μm. The acetone was not detected by gas chromatography.
Example 7
Paliperidone palmitate 10g was dissolved in 500mL ethanol to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 45 ℃ and setting the temperature of a nozzle to be 45 ℃; introducing carbon dioxide at a flow rate of 1L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 20MPa. Opening a high-pressure metering pump, setting the sampling rate of the paliperidone palmitate methanol solution to be 30mL/min, spraying the paliperidone palmitate solution into the crystallization kettle through a nozzle at the top of the crystallization kettle by the high-pressure metering pump, and after the paliperidone palmitate ethanol solution is completely added, closing the high-pressure metering pump, and continuously introducing carbon dioxide for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, collecting and obtaining 8.7g of white paliperidone palmitate nanocrystals, and detecting the particle size distribution by a Markov laser particle sizer: d (D) 10 0.3μm,D 50 1.0μm,D 90 2.5μm。
Example 8
Paliperidone palmitate 10g was dissolved in 1000mL ethanol to give a paliperidone palmitate solution. Opening a supercritical crystallization device, setting the temperature of a crystallization kettle to be 50 ℃ and setting the temperature of a nozzle to be 50 ℃; introducing carbon dioxide at a flow rate of 2L/min, and regulating a back pressure valve to maintain the pressure of the crystallization kettle at 20MPa. Opening a high-pressure metering pump, setting the sampling rate of the paliperidone palmitate methanol solution to be 60mL/min, spraying the paliperidone palmitate solution into the crystallization kettle through a nozzle at the top of the crystallization kettle by the high-pressure metering pump, and after the paliperidone palmitate ethanol solution is completely added, closing the high-pressure metering pump, and continuously introducing carbon dioxide for 30min. Stopping introducing carbon dioxide, opening an exhaust valve to release pressure to normal pressure, opening a crystallization kettle, collecting and obtaining 8.6g of white paliperidone palmitate nanocrystals, and detecting the particle size distribution by a Markov laser particle sizer: d (D) 10 0.4μm,D 50 1.1μm,D 90 2.9μm。
Example 9
80mL of water for injection is added into a container made of stainless steel, 0.20g of citric acid, 0.20g of disodium hydrogen phosphate, 0.11g of sodium hydroxide and 40001.20g of polyvinyl alcohol are sequentially added, and the mixture is fully stirred and mixed until the mixture is completely dissolved, so as to obtain an auxiliary material mixed solution. 8.0g of paliperidone palmitate nanocrystals prepared in examples 1-8 were added to the above adjuvant mixture and thoroughly mixed, respectively, to obtain 8 uniformly dispersed paliperidone palmitate nanocrystal suspensions. Canning into a syringe to prepare the paliperidone palmitate nanocrystalline suspension injection with the specification of 100 mg/mL.
Example 10
80mL of water for injection is added into a container made of stainless steel, 0.28g of citric acid, 0.28g of disodium hydrogen phosphate, 0.15g of sodium hydroxide and 40001.68g of polyvinyl alcohol are sequentially added, and the mixture is fully stirred and mixed until the mixture is completely dissolved, so as to obtain an auxiliary material mixed solution. 8.0g of paliperidone palmitate nanocrystals prepared in examples 1-8 were added to the above adjuvant mixture and thoroughly mixed, respectively, to obtain 8 uniformly dispersed paliperidone palmitate nanocrystal suspensions. Canning into a syringe to prepare the paliperidone palmitate nanocrystalline suspension injection with the specification of 100 mg/mL.
The foregoing is merely a preferred embodiment of the present invention and it should be noted that modifications and adaptations to those skilled in the art may be made without departing from the principles of the present invention, which are intended to be comprehended within the scope of the present invention.
Claims (10)
1. A method for preparing paliperidone palmitate nanocrystals, comprising the steps of:
and dissolving paliperidone palmitate in an organic solvent, and performing carbon dioxide supercritical crystallization on the paliperidone palmitate solution to obtain paliperidone palmitate nanocrystals.
2. The method of preparing of claim 1, wherein the paliperidone palmitate solution has a concentration of 10-100 g/mL;
the organic solvent comprises one or more of methanol, ethanol and acetone.
3. The method according to claim 1, wherein the supercritical carbon dioxide crystallization specifically comprises: introducing carbon dioxide into a crystallization kettle, spraying paliperidone palmitate solution into the crystallization kettle through a nozzle positioned at the top of the crystallization kettle, and performing supercritical carbon dioxide crystallization.
4. The process according to claim 3, wherein the crystallization kettle is at a temperature of 35 to 55℃and a pressure of 10 to 30MPa.
5. A method of manufacture according to claim 3, wherein the temperature of the nozzle is 40-45 ℃.
6. The method of claim 3, wherein the continuous carbon dioxide introduction time is 30 to 60 minutes after the paliperidone palmitate solution is stopped being injected.
7. The method of preparing of claim 3 or 6, wherein the flow rate ratio of paliperidone palmitate solution to carbon dioxide is 15 to 60:1.
8. paliperidone palmitate nanocrystals prepared by the preparation method of any one of claims 1 to 7, having a particle size distribution range of: d (D) 10 Is 0.3-0.6 mu m, D 50 Is 0.9-1.4 mu m, D 90 2.0-4.4 μm.
9. The paliperidone palmitate nanocrystalline suspension injection is characterized by comprising the following components in parts by weight: the paliperidone palmitate nanocrystal of claim 8, 100 parts, 2.5-3.5 parts of citric acid, 2.5-3.5 parts of disodium hydrogen phosphate, 1.4-1.9 parts of sodium hydroxide, 15-21 parts of polyvinyl alcohol and 1000-1100 parts of water for injection.
10. The method for preparing paliperidone palmitate nanocrystalline suspension injection as defined in claim 9, comprising the steps of:
mixing citric acid, disodium hydrogen phosphate, sodium hydroxide, polyvinyl alcohol and water for injection to obtain an auxiliary material mixed solution;
and mixing the auxiliary material mixed solution with paliperidone palmitate nanocrystals to obtain paliperidone palmitate nanocrystal suspension injection.
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