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WO2018228441A1 - Controlled release pharmaceutical composition and method for preparing same - Google Patents

Controlled release pharmaceutical composition and method for preparing same Download PDF

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Publication number
WO2018228441A1
WO2018228441A1 PCT/CN2018/091103 CN2018091103W WO2018228441A1 WO 2018228441 A1 WO2018228441 A1 WO 2018228441A1 CN 2018091103 W CN2018091103 W CN 2018091103W WO 2018228441 A1 WO2018228441 A1 WO 2018228441A1
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WO
WIPO (PCT)
Prior art keywords
hydrochloride
controlled release
pharmaceutical composition
composition according
release pharmaceutical
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Application number
PCT/CN2018/091103
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French (fr)
Chinese (zh)
Inventor
王捷
王立坤
顾国祥
张凤娥
Original Assignee
江苏恒瑞医药股份有限公司
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Priority to CN201880008336.9A priority Critical patent/CN110214007A/en
Publication of WO2018228441A1 publication Critical patent/WO2018228441A1/en

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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
    • A61K9/0012Galenical forms characterised by the site of application
    • A61K9/0053Mouth and digestive tract, i.e. intraoral and peroral administration
    • A61K9/0065Forms with gastric retention, e.g. floating on gastric juice, adhering to gastric mucosa, expanding to prevent passage through the pylorus
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2022Organic macromolecular compounds
    • A61K9/2027Organic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyvinyl pyrrolidone, poly(meth)acrylates
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2022Organic macromolecular compounds
    • A61K9/205Polysaccharides, e.g. alginate, gums; Cyclodextrin
    • A61K9/2054Cellulose; Cellulose derivatives, e.g. hydroxypropyl methylcellulose
    • 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
    • A61K9/4841Filling excipients; Inactive ingredients
    • A61K9/4866Organic macromolecular compounds

Definitions

  • the invention relates to a controlled release pharmaceutical composition, belonging to the field of pharmacy.
  • a controlled release formulation such as the cardro-dualopa modified release formulation disclosed in CN101910113A.
  • the oral gastric retention preparation prolongs the residence time of the drug at the upper end of the gastrointestinal tract, and even if the drug is poorly absorbed at the rear end of the intestinal tract, the drug can be effectively released and absorbed after 6 hours of administration.
  • the dosing interval and dose increase patient compliance.
  • the gastric floating preparation is one of the ways of gastric retention, which increases the residence time of the preparation in the stomach.
  • CN103037850A discloses a type of elongated intragastric retention capsule, which has been shown to prolong gastric retention time, however, such a design There is a risk of gastric obstruction or permanent retention of the system, so its actual value is small.
  • a large number of drugs have been made into a gastric floating drug delivery system combining immediate release and controlled release, but most of them are double-layer tablets or capsules.
  • Yin Lifang et al. disclose a gastric floating system.
  • the bilayer tablet has active ingredients of pioglitazone and metformin, wherein the immediate release component is pioglitazone and the controlled release component is metformin.
  • the bilayer tablet is obtained by adding sodium carbonate which can generate carbon dioxide and a low density floating aid stearyl alcohol. The effect of floating is achieved, with the most preferred formulation being able to float in the test solvent for at least 24 h (International Journal of Pharmaceutics 476 (2014) 223-231).
  • single tablets have various disadvantages such as poor floating ability, long drift time, and large individual differences.
  • Indian Patent Application No. 200900/00792 A discloses a dual particle intragastric delivery system comprising immediate release particles of ofloxacin and gastric floating controlled release particles, wherein the controlled release particles comprise a hydrophobic material and a hydrophilic material.
  • Hot melt extrusion is the process of pumping raw materials through a mold through a mold at a high temperature to a uniform shape product.
  • HME has many advantages over other drug treatment techniques in that the molten polymer can be used as a thermal adhesive during extrusion and as a drug depot and/or drug release blocker upon cooling and solidification. Since the process does not require solvent and water, the number of processing steps is reduced and the time consuming drying step is eliminated.
  • the matrix material can be assembled into larger units that are independent of the compression characteristics. The intense mixing and agitation exerted by the rotating screw causes the agglomeration of suspended particles in the molten polymer to make the dispersion more uniform.
  • Nakamichi et al. disclose a floating preparation of nicardipine hydrochloride prepared by a twin-screw extruder, which is hot melt extruded.
  • the polymer material was hydroxypropylmethylcellulose acetate succinate (HPMCAS). It was found that only the use of drugs and polymers did not result in a loose extrudate, and the third intermediate substance, dihydrate phosphoric acid, must be added. Calcium, when the amount of calcium phosphate dihydrate is 8%, floats in gastric juice for 6 hours (International Journal of Pharmace-Utics 218 (2001) 103-112).
  • US2016113906A discloses a hot melt extruded composition which, by adding a polar organic solvent to a hot melt extruded composition, reduces the decomposition of the active ingredient and increases the miscibility between the active ingredient and the polymer. Reduces the operating temperature and temperature of the hot melt extrusion and reduces the torque.
  • Nakamichi et al. examined the effect of moisture on solid dispersions prepared by twin-screw hot melt extruders. The results of the tests demonstrate that the addition of water reduces the flow temperature (Tfb) of the material, demonstrating that the material can be at temperatures below the melting point. Extrusion (International Journal of Pharmaceutics 241 (2002) 203-211).
  • Padma V. Devarajan et al. disclose a gastric floating controlled release multiparticulate formulation of metoprolol succinate prepared by hot melt extrusion to optimize the hot melt extruded material Eudragit RSPO The ratio between polyoxyethylene (PEO) and hydroxypropylmethylcellulose (HPMC) is used to balance the floating capacity and the controlled release ability, and the production of gas uses sodium carbonate (International Journal of Pharmaceutics 491 (2015) 345-351).
  • PEO polyoxyethylene
  • HPMC hydroxypropylmethylcellulose
  • Mamoru Fukuda et al. disclose a gastric retention floating sheet prepared by hot melt extrusion using Eudragit RSPO ( RS PO) and or Eudragit EPO ( E PO.) Matrix material, the effect of sodium carbonate on the physicochemical properties of the composition was examined (Journal of Controlled Release 115 (2006) 121-129).
  • the invention provides a controlled release pharmaceutical composition prepared by hot melt extrusion, which effectively prolongs the residence time in the gastrointestinal tract and increases the effective absorption time of the gastrointestinal tract to more than 10 hours, thereby effectively reducing the dosage. The number of times increases the compliance of patients taking medication.
  • the present invention provides a controlled release pharmaceutical composition
  • a controlled release pharmaceutical composition comprising: a) an immediate release component comprising an active drug, b) a delayed release floating component comprising an active drug, characterized in that said delayed release floating component is passed through a heat fusion The extrusion process is prepared.
  • the controlled release pharmaceutical composition of the present invention is characterized in that the delayed release floating component contains at least one enteric polymer.
  • the delayed release drug component containing the enteric polymer of the present invention releases the drug at a pH of ⁇ 5.5.
  • the controlled release pharmaceutical composition provided by the present invention is characterized in that the enteric polymer is selected from the group consisting of polyvinyl alcohol acetate phthalate, cellulose acetate phthalate, and 1,2,4-benzenetricarboxylic acid acetic acid.
  • the methacrylic acid-ethyl acrylate copolymer is a 1:1 copolymer corresponding to commercially available Eudragit 100-55 or Kollicoat MAE 100P.
  • the methyl vinyl ether-maleic anhydride copolymer is commercially available. series.
  • the methacrylic acid-methyl methacrylate copolymer is a 1:1 or 1:2 copolymer corresponding to Eudragit L100 and Eudragit S100, respectively.
  • the mixture of polyvinyl acetate and polyvinylpyrrolidone K30 is Kollidon SR.
  • the enteric polymer described herein is an Eudragit polymer, such as Eudragit L, Eudragit S or Eudragit L 100-55.
  • the enteric polymer described in the present invention is hydroxypropyl methylcellulose acetate succinate (HPMCAS), hydroxypropyl methyl acetate succinate disclosed in the prior art US 4,266,981 B, CN 104208713 A, and CN 103153343 A. Cellulose is included within the scope of this application.
  • HPMCAS sold by Shin-Etsu Chemical Co., Ltd. (Tokyo, Japan) is classified into three grades having different combinations of substituent levels to provide enteric protection at various pH levels.
  • AS-LF and AS-LG grades (“F” means fine and "G” means granules) provide enteric protection at a pH of up to 5.5.
  • the AS-MF and AS-MG grades provide enteric protection at pH values up to 6.0, while the AS-HF and AS-HG grades provide enteric protection at pHs up to 6.8.
  • the controlled release pharmaceutical composition provided by the present invention is characterized in that the ratio of the active drug to the enteric polymer in the delayed release floating component is selected from 1:0.1 to 1:100, preferably from 1:0.1 to 1:50, more preferably 1: 1-1:25.
  • the controlled release pharmaceutical composition provided by the present invention wherein the hot melt extrusion method optionally participates in a hot melt extrusion process, that is, in some embodiments, a solvent is added, and in other embodiments, a solvent is not added, in the present invention
  • a solvent is added, and in other embodiments, a solvent is not added, in the present invention
  • the participation of the solvent means that the solvent is added before the hot melt extrusion or during the hot melt extrusion process for the needs of the invention.
  • the solvent only needs to be able to be volatilized after the end of the hot melt extrusion process.
  • the present invention limits the boiling point of the solvent to 30. -110 ° C.
  • the controlled release pharmaceutical composition provided by the present invention is characterized in that the solvent is at least selected from the group consisting of water, methanol, ethanol, isopropanol, acetone, pentane, hexane, heptane, cyclohexane, dichloromethane, tetrahydrofuran.
  • the solvent is at least selected from the group consisting of water, methanol, ethanol, isopropanol, acetone, pentane, hexane, heptane, cyclohexane, dichloromethane, tetrahydrofuran.
  • One is preferably water and ethanol.
  • the present invention provides a controlled release pharmaceutical composition having a density of delayed release floating components in a controlled release pharmaceutical composition of from 0.1 to 1.0 g/cm3, preferably from 0.2 to 0.8 g/cm3, when a solvent is involved in the hot melt extrusion process. Most preferably, it is 0.3-0.7 g/cm3, which is porous under electron microscopy, and can be floated immediately in a solution of FaSSGF at pH 5.0 and maintained for a float time of more than 24 h.
  • the controlled release pharmaceutical composition provided by the present invention contains an alkaline substance which is exposed to an acid generating gas in the preparation process without adding a solvent, that is, the alkaline substance in the controlled release pharmaceutical composition of the present invention is not essential, and when the alkaline substance is contained
  • the basic substance is specifically an alkali metal carbonate, an alkali metal or an alkaline earth metal hydrogencarbonate, more specifically sodium hydrogencarbonate, sodium carbonate, sodium aminoacetate carbonate, potassium hydrogencarbonate, magnesium carbonate and calcium carbonate.
  • the controlled release pharmaceutical composition provided by the present invention does not contain calcium phosphate dihydrate, Nakamichi (International Journal of Pharmace-Utics 218 (2001) 103-112), and others add calcium phosphate dihydrate to the drug and the matrix, and by hot melt extrusion After that, a floatant was prepared.
  • the controlled release pharmaceutical composition provided by the present invention is less than 30%, more preferably less than 20% Most preferably less than 10%.
  • the controlled release pharmaceutical composition of the present invention is characterized in that the delayed release floating component is in a multi-unit form.
  • the controlled release pharmaceutical composition of the present invention is characterized in that the multi unit form is a microtablet, a pellet, a pellet, preferably a pellet.
  • the immediate release component of the controlled release pharmaceutical composition provided by the invention may be selected from the form of pellets, microtablets, granules and the like. Specifically, when the immediate release component is a pellet, the active drug and the blank pellet core may be contained. .
  • sustained-release preparation In general, pharmaceutical preparations reach the colon in most cases after oral administration in 3 to 6 hours. Therefore, the success of the sustained-release preparation is to increase the time of gastrointestinal absorption and increase absorption.
  • the Biopharmaceutical Classification System introduced by the FDA has classified drugs according to their solubility and intestinal permeability, see "The Biopharmaceutics Classification System (BCS) Guidance”. Jennifer B. Dressman and Christos Reppas, on page 273 of the Oral Drug Absorption: Prediction and Assessment, mention that drugs that have high solubility and permeability when administered orally (Class I) generally have good absorption throughout the gastrointestinal tract. It is the most preferred drug for the sustained release preparation, and such a drug is included in the range of the active drug of the delayed release floating component of the present invention.
  • Class I drugs in the BCS classification of the present invention include, but are not limited to, pabitatin, Cobimetinib, Patiromer, omarigliptin, bupropion, guanfacine, venlafaxine hydrochloride, methylphenidate hydrochloride, Tetrazolamide, flurbanin, eliglustat, alogliptin, dimethyl fumarate, pyrenoprene, lometanide, rosobinib, clozaban, dalfampridine, Prolia, drone Dalong hydrochloride, Pralatrexate, lacosamide, fesoterodine fumarate, alprazolam, amitriptyline hydrochloride, amlodipine besylate, benazepril, amoxicillin, anastrozole, azastroz Ting, bisoprolol, buspirone, caffeine, carbidopa, cetirizine, chloroquine
  • the composition of the present invention effectively uses the enteric polymerization to effectively prolong the residence time of the drug in the gastrointestinal tract due to the use of hot melt extrusion technology and gastric floating technology, especially the use of enteric polymerization.
  • the absorption rate of the drug in the small intestine shows a better effect for the drug of this kind.
  • the BCS classification of the present invention belongs to the class II to IV drugs including, but not limited to, febuxostat, ixazomib, Alectinib, Erismodegib, vandetanib, aprepitant, worapsar sulfate, aspirin, metformin, Engliflozin, linagliptin, naltrexone, dasabuvir, sofosbuvir, amphetamine, etravirine, everolimus, itraconazole, vemurafenib, telaprevir , tacrolimus, posaconazole, isikato, redipavir, Suvorexant, Ombitasvir, paritaprevir, daclatasvir, cariprazine, brexpiprazole, omemiprofen, levetiracetam, ivacaftor, eluxadoline , lumacaftor, ivacaftor
  • the controlled release pharmaceutical composition provided by the present invention is characterized in that the delayed release floating component further comprises at least one plasticizer selected from the group consisting of triethyl citrate and tributyl citrate. , polyethylene glycol, triethyl phthalate, tributyl phthalate, dibutyl sebacate, diethyl sebacate, glyceryl stearate, diethyl succinate, propylene glycol , castor oil and triacetin, preferably triethyl citrate, the plasticizer is present in an amount of from 0.01% to 50%, preferably from 0.1% to 30%, most preferably from 2.5% to 15% (% by mass, by solids) The total mass of the components is calculated as 100).
  • the plasticizer is present in an amount of from 0.01% to 50%, preferably from 0.1% to 30%, most preferably from 2.5% to 15% (% by mass, by solids) The total mass of the components is calculated as 100).
  • the immediate release component and/or the controlled release floating component of the controlled release pharmaceutical composition provided herein further comprises at least one pharmaceutically acceptable additional excipient, a pharmaceutically acceptable excipient
  • additional excipient include, but are not limited to, fillers, lubricants, glidants, binders, disintegrants.
  • excipients are conventionally incorporated into solid dosage forms to facilitate ease of handling and to improve the performance of the dosage form.
  • Common excipients include diluents or fillers, lubricants, glidants, binders, disintegrants, and the like. Wherein a diluent or filler is added to increase the weight of the individual dose to a size suitable for tablet compression.
  • Suitable diluents include powdered sugar, calcium phosphate, calcium sulfate, microcrystalline cellulose, lactose, mannitol, kaolin, sodium chloride, dried starch, sorbitol, and the like.
  • the lubricant reduces the friction between the particles and the mold wall during compression and discharge. This prevents the particles from adhering to the tablet punches, facilitating their discharge from the tablet press, and the like.
  • suitable lubricants include, but are not limited to, talc, stearic acid, vegetable oils, calcium stearate, zinc stearate, magnesium stearate, and the like.
  • Glidants are used to improve the flow characteristics of the particles.
  • suitable glidants include, but are not limited to, silica, corn starch, micronized silica gel, talc, polyethylene glycol.
  • a binder is usually used, and examples of suitable binders include, but are not limited to, pyrrolidone, polyvinylpyrrolidone, xanthan gum, cellulose gum such as carboxymethylcellulose, methyl Cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropyl methylcellulose, hydroxy cellulose, gelatin, starch and pregelatinized starch.
  • the disintegrant refers to a substance which can rapidly break up a tablet into fine particles in a gastrointestinal fluid, so that the functional component dissolves and absorbs rapidly, and functions.
  • the disintegrants described in the present invention include, but are not limited to, one or more of low-substituted hydroxypropylcellulose, croscarmellose sodium, sodium carboxymethyl starch, and crospovidone.
  • compositions provided herein include, but are not limited to, preservatives, antioxidants, or any other excipients commonly used in the pharmaceutical industry, and the like.
  • compositions provided by the present invention are ultimately presented in a pharmaceutically acceptable form for administration to a patient, optionally as a tablet or capsule.
  • the recommended mode of administration of the controlled release compositions of the present invention is after meals.
  • the controlled release pharmaceutical composition of the present invention is characterized in that the active drug in the delayed release floating composition optionally remains in a crystalline state or is converted to an amorphous state after the hot melt extrusion process.
  • compositions of the present invention may include more than one drug, ie, The immediate release component is the same as or different from the drug in the delayed release release component.
  • the present invention also provides a method of preparing the above controlled release drug combination.
  • the method for preparing a controlled release pharmaceutical composition comprises the steps of: 1) premixing at least one solvent, an active ingredient in a delayed release floating component, and at least one enteric polymer before hot melt extrusion.
  • at least one solvent, the active ingredient in the delayed release floating component and the at least one enteric polymer are mixed in advance to obtain a premixed crude product; 2) the premixed crude product passes through the heating screw zone of the extruder. After the die exits the extrudate.
  • the preparation method provided by the present invention is characterized in that the solvent only needs to satisfy the fact that it can be volatilized after the end of the hot melt extrusion process.
  • the present invention limits the boiling point of the solvent to 30-110 °C.
  • the preparation method provided by the present invention is characterized in that the solvent is selected from the group consisting of water, methanol, ethanol, isopropanol, acetone, pentane, hexane, heptane, cyclohexane, dichloromethane, tetrahydrofuran, preferably water, ethanol. , isopropanol.
  • the solvent is used in an amount of from 0.1% to 70%, preferably from 1% to 50%, most preferably from 10% to 30% by mass based on the total mass of the solid component of 100.
  • the temperature of the heated zone at the front end of the die should be greater than the glass transition temperature (Tg) of the extruded mixture.
  • the preparation method provided by the present invention is characterized in that the die temperature is from 70 to 200 ° C, preferably from 90 to 180 ° C, more preferably from 110 to 160 ° C.
  • the preparation method provided by the present invention is characterized in that the solvent injection screw zone temperature is 10-90 °C.
  • the esters including lactones
  • amides including lactones
  • the preparation method provided by the present invention is characterized by further comprising the steps of: 1) cooling the extrudate, 2) removing the extrudate from the solvent; 3) cutting the extrudate.
  • the solvent having a low boiling point and being relatively volatile may be substantially volatilized during extrusion according to the nature of the solvent itself and the temperature of the die, and the solvent having a low boiling point and being volatile is included, but not limited to, ethanol.
  • Substantially volatilized as used herein means that the residual amount of solvent in the extrudate is less than 15%, preferably less than 12%, and most preferably less than 10%.
  • the method provided by the present invention when a solvent having a higher boiling point is selected, may be followed by a step of desolvating the extrudate after the end of hot melt extrusion.
  • the solvent in the extrudate is removed under elevated temperature and/or vacuum conditions.
  • the elevated temperature is sufficient to convert the solvent from a liquid to a gaseous state.
  • the solvent in the extrudate is removed under reduced pressure conditions.
  • the method of preparation provided by the present invention further comprises the step of cooling the extrudate.
  • the present invention provides a method of preparing a controlled release floating component in a controlled release pharmaceutical composition, characterized by further comprising the step of cutting the extrudate.
  • the preparation method of the immediate release portion of the present invention includes wet granulation, dry granulation, powder direct pressing and the like.
  • the preparation method provided by the present invention is characterized in that the extruder is selected from the group consisting of a single screw hot melt extruder, an intermeshing screw extruder, a twin screw hot melt extruder, preferably a twin screw hot melt extruder.
  • delayed release refers to a type of improved release wherein the pharmaceutical dosage form exhibits a time delay between oral administration of the pharmaceutical dosage form and release of the drug from the dosage form.
  • the delayed release release dosage form will have little or no release of the active compound for a predetermined period of time or until predetermined conditions are met, such as exposure to a certain pH level, and then the release of the active compound occurs immediately thereafter.
  • controlled release in the context of the invention refers to a type of extended release formulation wherein the gradual release of the drug is controlled or manipulated for an extended period of time.
  • Figure 23 Powder diffraction pattern of hydrochlorothiazide before and after extrusion of Example 20.
  • HPMCAS used in the examples of the present invention was purchased from Shin-Etsu Chemical Co., Ltd., and the hot melt extruder was Thermo Fisher's twin-screw hot melt extrusion instrument.
  • the single capsule comprises an immediate release component and a delayed release floating component
  • the immediate release component is a microtablet containing 8 mg of febuxostat active ingredient
  • the delayed release floating component is a particulate A containing 32 mg of febuxostat active ingredient, granules A is released above pH 6.
  • the immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is listed in Table 1 below.
  • the specific preparation process wet granulation mechanism granules, mixing raw materials and auxiliary materials, adding binder, stirring, 1500 rpm cutting, sieving, drying, to moisture ⁇ 3%, passing through 30 mesh sieve, and then using Chuangbo C&C600B single Stamping machine, 4.76mm punch press. Tablet weight: theory 61.5mg, the actual control is 59-65mg, the hardness is about 30N.
  • the febuxostat bleaching granule A was prepared by a hot melt extrusion process, the formulation of which is listed in Table 2 below.
  • the febuxostat and HPMCAS MG were weighed and mixed uniformly in a blender, and the hot melt extruder (Simofly) was set as shown in Table 3.
  • the speed is 700 ul/min
  • Zone 2 feeding the speed is 4 g/min
  • the rotation speed of the screw is set to 100 rpm
  • the extrudate is cut into segments, and then the extrudate is oven-dried at 60 ° C for 2 h.
  • the ethanol content is less than 0.5%, and is pulverized to 2 mm after drying.
  • a single capsule contains an immediate release component and a delayed release floating component
  • the immediate release component is a pellet containing 8 mg of febuxostat active ingredient
  • the remainder of the capsule contains a delayed release of febuxostat containing 32 mg of febuxostat.
  • Floating particles B this delayed release of floating enteric particles B is rapidly released above pH 6.
  • the immediate release febuxostat pellets were prepared by a blank pellet core drug preparation process, and the prescription composition is shown in Table 4.
  • the febuxostat controlled release floating granules B were prepared by a hot melt extrusion process, and the formulation composition thereof is shown in Table 5.
  • febuxostat 150 g of febuxostat and 90 g of HPMCAS MG and 360 g of hydroxypropylmethylcellulose were weighed and mixed uniformly in a blender.
  • the temperature setting of the hot melt extruder was as shown in Table 3.
  • the ethanol was added to the Zone 4 of the hot melt extruder at a speed of 700 ul/min, the Zone 2 was fed at a speed of 4 g/min, and the rotation speed of the screw was set to 100 rpm. After cutting into sections, the extrudate was oven-dried at 60 ° C for 2 h, and the ethanol content was ⁇ 0.5%. After drying, it is pulverized to 4 mm, and the controlled release granule B of febuxostat is obtained.
  • the single capsule comprises an immediate release component and a controlled release floating component
  • the immediate release component is a microtablet containing 8 mg of febuxostat
  • the remainder of the capsule comprises a total of 32 mg of febuxostat gastric floating particles C, the gastric floating particles C is released above pH 5.
  • the immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is listed in Table 1 above.
  • the febuxostat controlled release floating granule C was prepared by a hot melt extrusion process, and its prescription composition is shown in Table 6.
  • hot melt extrusion was carried out, and the temperature parameter setting was the same as that of the preparation of the pellet A.
  • the hot melt extruder's Zone4 was added with ethanol at a speed of 600 ul/min, Zone 2 was fed at a speed of 2 g/min, the screw speed was 60 rpm, the extrudate was cut into segments, and the extrudate was oven dried at 60 ° C for 2 h.
  • the ethanol content is ⁇ 0.5%, and after pulverization, it is pulverized to 4 mm long particles, and the febuxostat floating particles C are obtained.
  • Example 4 is a febuxostat formulation consisting of 40% immediate release febuxostat microtablets and 60% febuxostat floating particles C which release the drug above pH 5
  • the single capsule contains an immediate release component and a controlled release floating component
  • the immediate release component is a microchip containing 16 mg of febuxostat
  • the remainder of the capsule contains a total of 24 mg of febuxostat delayed release floating particle C, which is delayed release.
  • the floating controlled release granule C is released above pH 5.
  • the immediate release febuxostat microchip was prepared by a wet granulation process, the formulation of which is listed in Table 1 above, and the febuxostat controlled release floating granule C was the same as in Example 3.
  • Example 5 a febuxostat formulation consisting of immediate release febuxostat pellets and delayed release febuxostat floating particles D 5
  • a single capsule contains an immediate release component and a controlled release floating component.
  • the immediate release component is a pellet containing 8 mg of febuxostat active ingredient, and the remainder of the capsule contains a delay of 32 mg of febuxostat containing 32 mg of febuxostat.
  • the floating particles D are released, and the gastric floating delayed release particles D are slowly released while floating in the gastric juice.
  • the immediate release febuxostat pellets were prepared by a blank pellet core drug preparation process, and the prescription compositions are listed in Table 4 above.
  • the febuxostat gastric floating controlled release granule D was prepared by a hot melt extrusion process, and the composition of the formulation is shown in Table 7.
  • the febuxostat After blending the febuxostat with the quaternary amino methacrylate copolymer type B and hypromellose, it was sheared in a wet granulator while slowly adding triethyl citrate dropwise.
  • the mixed materials were hot melt extruded, the temperature parameters were set as in Table 3, ethanol was added in Zone 4, the speed was 1000 ul/min, Zone 2 was fed, the speed was 4 g/min, the screw speed was set to 100 rpm, and the extrusion was performed.
  • the material was cut into sections, and then the extrudate was oven-dried at 60 ° C for 2 h, and the ethanol content was ⁇ 0.5%. After drying, it is pulverized to 4 mm long granules, and the controlled release granule D of febuxostat is obtained.
  • Example 6 is a non-busestat formulation consisting of an immediate release febuxostat microparticle and a delayed release of febuxostat floating particle E 6
  • the single capsule contains an immediate release component and a controlled release floating component.
  • the immediate release component is a microtablet containing 8 mg of febuxostat.
  • the remainder of the capsule contains a total of 32 mg of febuxostat delayed release floating particles E, which floats on the stomach.
  • the controlled release granule E is slowly released while floating in the gastric juice.
  • the immediate release febuxostat microchips were prepared by a wet granulation process, and the formulation of the compositions is shown in Table 1.
  • the febuxostat gastric floating delayed release granule E was prepared by a hot melt extrusion process, and its prescription composition is shown in Table 8.
  • the febuxostat was mixed with other excipients in a prescribed amount and then subjected to hot melt extrusion.
  • the temperature parameters were set as shown in Table 3.
  • the content is ⁇ 0.5%, pulverized to 4 mm long particles, and the obtained bupretaxer gastric floating controlled release granule E is obtained.
  • Example 7 is a non-busestat formulation consisting of an immediate release febuxostat microparticle and a controlled release febuxostat floating particle F
  • the single capsule contains the immediate release component and the controlled release floating component, and the immediate release component is a microchip containing 8 mg of febuxostat.
  • the remainder of the capsule contains a total of 32 mg of febuxostat floating particles F, which is controlled by the stomach.
  • the release granule E is slowly released while floating in the gastric juice.
  • the immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is listed in Table 1.
  • the febuxostat gastric floating controlled release granule F was prepared by a hot melt extrusion process, and its formulation composition is shown in Table 9.
  • the febuxostat was mixed with other excipients in a prescribed amount and then subjected to hot melt extrusion.
  • the temperature parameters were set as shown in Table 3.
  • the content is ⁇ 0.5%, and after pulverization, it is pulverized to 4 mm long particles, and the controlled release granule F of febuxostat is obtained.
  • Example 8 is a febuxostat formulation consisting of an immediate release febuxostat microplatelet and a febuxostat floating particle G which releases the drug above pH 5.5.
  • the single capsule comprises an immediate release component and a delayed release floating component
  • the immediate release component is a microtablet containing 8 mg of febuxostat active ingredient
  • the delayed release floating component is a particulate G containing 32 mg of febuxostat active ingredient, granules A is released above pH 5.5.
  • the immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is shown in Table 1, and the formulation of febuxostat delayed release floating granules G is shown in Table 10.
  • Table 11 The hot melt extrusion and temperature settings are shown in Table 11.
  • Zone4 is added with water, the feeding speed is 5g/min, the watering speed is 0.9ml/min, the screw rotation speed is set to 100rpm, the extrudate is cut into segments, and the extrudate is dried in an oven at 60°C for 2 hours. Moisture ⁇ 3%, pulverized to 2 mm after drying, test density was 0.5 g/cm 3 , and the obtained febuxostat granule G and the febuxostat microderage obtained in Example 1 were filled into capsules to obtain febuxostat preparation. 8.
  • Example 12 The human pharmacokinetic study was carried out together with the preparations obtained in Example 3 and Example 4 using a commercially available 40 mg-sized febuxostat as a reference preparation, and the results of the study are shown in Table 12 below.
  • T max maximum blood concentration time
  • AUC 0 ⁇ drug time curve area
  • Example 3 and Example 4 can reduce the maximum peak concentration of the drug compared with the commercially available febuxostat reference preparation, greatly prolong the duration of action, and exert controlled release of the drug.
  • pH5.0FaSSGF 300mL of pH5.0FaSSGF was used as the dissolution medium to observe the floating condition of the gastric floating particles under simulated gastric fluid. After observation, all the particles immediately floated and floated for a long time. After 24 hours, the particles remained floating and stopped. Observed.
  • the rate of dissolution can indicate the rate at which the drug is released from the formulation in the gastrointestinal environment, and the lower rate of release response is a lower Cmax and longer release time on the pharmacokinetic data.
  • the dissolution rate of the preparation prepared in the present invention is remarkably lowered, and it can be inferred that the preparations of the present invention (Examples 1 to 7) can achieve a lower Cmax value than the immediate release tablets.
  • the traits of the particle G were observed by scanning electron microscopy, and it was found that the particle G was porous under the electron microscope, as shown in Fig. 5.
  • the powder diffraction pattern for the crystalline state of the febuxostat and the non-busestat after extrusion, as shown in Fig. 6, is maintained in a crystalline state after hot melt extrusion.
  • hydrochlorothiazide and HPMC AS LG were uniformly mixed and subjected to hot melt extrusion, and the temperature parameters were set as shown in Table 13 (° C.).
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 400 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The extrusion is smooth, the process is stable, the sample is expanded, and it can be quickly floated.
  • Hydrochlorothiazide and HPMCP were uniformly mixed and hot melt extruded.
  • the temperature parameters were set as shown in Table 14 (°C).
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 500 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The sample is extruded smoothly and can be quickly floated.
  • hydrochlorothiazide starting material and the crystal form test powder diffraction pattern of the hydrochlorothiazide after extrusion in Example 11 hydrochlorothiazide remained in a crystalline state after hot melt extrusion, as shown in FIG. 9; the dissolution profile of the formulation of Example 11 is shown in FIG. Shown.
  • Nifedipine and HPMC AS LG were uniformly mixed and hot melt extruded.
  • the temperature parameters were set as shown in Table 15 (°C).
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 1200 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The sample is extruded smoothly and can be quickly floated.
  • the tadalafil and HPMC AS LG were mixed uniformly for hot melt extrusion, and the temperature parameters were set as shown in Table 16 (°C).
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 900 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The extrusion is smooth, the process is stable, the sample is expanded, and it can be quickly floated.
  • Example 13 The powder diffraction pattern of the tadalafil raw material and the crystalline state of the tadalafil after extrusion in Example 13 was maintained, and the tadalafil remained in a crystalline state after hot melt extrusion, as shown in FIG. 13;
  • the dissolution profile of the formulation of Example 13 is shown in FIG.
  • the losartan and HPMC AS LG were uniformly mixed and hot melt extruded.
  • the temperature parameters were set as shown in Table 17 (°C).
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 600 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The extrusion is smooth, the sample is expanded, and it can be quickly floated.
  • the powder diffraction pattern of the losartan raw material and the crystalline state of losartan after extrusion in Example 14 was maintained, and the losartan remained in a crystalline state after hot melt extrusion, as shown in FIG. 15;
  • the dissolution profile is shown in Figure 16.
  • the dexamethasone and HPMC AS LG were mixed uniformly and hot melt extruded.
  • the temperature parameters were set as shown in Table 18 (°C).
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 400 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The extrusion is smooth, the sample is expanded, and it can be quickly floated.
  • the dexamethasone and HPMCP were uniformly mixed and hot melt extruded.
  • the temperature parameters were set as shown in Table 19 (°C).
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 400 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The extrusion is smooth, the surface of the sample expands, and the bubbles rupture on the surface, but can quickly float.
  • Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 600 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • Phenomenon The extrusion is smooth, the sample is expanded, and it can be quickly floated.
  • the febuxostat and HPMCP were uniformly mixed and hot melt extruded.
  • the temperature parameters were set as shown in Table 21 (°C).
  • Zone4 is added with water, the screw rotation speed is set to 100 rpm, the water adding speed is 700-900 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is ⁇ 3%, and the pulverization is 2 mm after drying.
  • the sample can expand and the sample can float.
  • Hydrochlorothiazide and HPMC AS LG were uniformly mixed and hot melt extruded.
  • the temperature parameters were set as shown in Table 22 (°C).
  • Zone2 feeding Zone2 plus ethanol
  • the screw rotation speed was set to 60 rpm
  • the ethanol speed was 700 ul/min
  • the extrudate was oven-dried at 60 ° C for 2 h
  • the moisture was ⁇ 3%
  • the pulverization was 2 mm after drying.
  • Phenomenon The extrusion is smooth, the process is stable, the sample is expanded, and it can be quickly floated.
  • hydrochlorothiazide starting material and the crystal form test powder diffraction pattern of the hydrochlorothiazide after extrusion in Example 19 hydrochlorothiazide remained in a crystalline state after hot melt extrusion, as shown in FIG. 21; the dissolution profile of the formulation of Example 19 is shown in FIG. Shown.
  • hydrochlorothiazide and HPMCP were uniformly mixed and subjected to hot melt extrusion, and the temperature parameters were set as shown in Table 23 (° C.).
  • Zone2 feeding Zone2 plus ethanol
  • the screw rotation speed was set to 50 rpm
  • the ethanol speed was 700 ul/min
  • the extrudate was oven-dried at 60 ° C for 2 h
  • the moisture was ⁇ 3%
  • the pulverization was 2 mm after drying.
  • Phenomenon The sample is extruded smoothly and can be quickly floated.
  • the losartan and HPMC AS LG were mixed uniformly for hot melt extrusion, and the temperature parameters were set as shown in Table 24 (°C).
  • Zone2 feeding Zone2 plus ethanol
  • the screw rotation speed was set to 50 rpm
  • the ethanol speed was 700 ul/min
  • the extrudate was oven-dried at 60 ° C for 2 h
  • the moisture was ⁇ 3%
  • the pulverization was 2 mm after drying.
  • Phenomenon The sample is extruded smoothly and can be quickly floated.
  • the powder diffraction pattern of the losartan raw material and the crystal form state of losartan after extrusion in Example 21 was maintained, and the losartan remained in a crystalline state after hot melt extrusion, as shown in FIG. 25;
  • the dissolution profile is shown in Figure 26.
  • the febuxostat and HPMCP were uniformly mixed and hot melt extruded.
  • the temperature parameters were set as shown in Table 25 (°C).
  • the Zone2 feed, Zone4 plus ethanol, the screw rotation speed was set to 50 rpm, the ethanol speed was 700/min, the extrudate was oven-dried at 60 ° C for 2 h, the moisture was ⁇ 3%, and the pulverization was 2 mm after drying.
  • the sample can expand and the sample can float.

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Abstract

The present application relates to a controlled release pharmaceutical composition. The controlled release pharmaceutical composition comprises: a) an immediate release component containing an active drug; and b) a delayed release floating component containing an active drug, the delayed release floating component is prepared by means of hot melt extrusion.

Description

一种控释药物组合物及其制备方法Controlled release pharmaceutical composition and preparation method thereof
本申请要求申请日为2017年6月14日的中国专利申请CN201710454301.5的优先权。本申请引用上述中国专利申请的全文。The present application claims priority on Chinese Patent Application No. CN201710454301.5, filed on Jun. 14, 2017. This application cites the entire text of the above-mentioned Chinese patent application.
技术领域Technical field
本发明涉及一种控释药物组合物,属于制药领域。The invention relates to a controlled release pharmaceutical composition, belonging to the field of pharmacy.
背景技术Background technique
在制药领域,为有效减少用药次数,增加患者服药的依从性,提高用药安全及降低胃肠道的副反应等目的,目前已经有不少药品被开发为含有速释组分及缓释组分的的控释制剂,例如CN101910113A中公开的卡左双多巴控释制剂。In the pharmaceutical field, in order to effectively reduce the number of medications, increase the compliance of patients taking medication, improve the safety of medication and reduce side effects of the gastrointestinal tract, many drugs have been developed to contain immediate release components and sustained release components. A controlled release formulation, such as the cardro-dualopa modified release formulation disclosed in CN101910113A.
大部分化合物在肠道的后端吸收差,导致患者服用制剂后,制剂在被转运至结肠段(一般认为是4-6小时)后,制剂无法进行有效的释放和吸收,对于清除快的药物,无法通过普通缓释的方式保证在服药后6小时能有效的维持血药浓度。口服的胃部滞留制剂在胃肠道的上端延长了药物的停留时间,即使针对在肠道后端吸收差,清除快的药物,也能保证在服药6小时后能够有效的释放和吸收,降低了给药间隔及剂量,提高了患者的依从性。胃漂浮制剂做为胃滞留的方式之一,增加了制剂在胃部的停留时间,以往于在胃肠道上端吸收但其溶解度很小或在碱性环境中易降解的药物,以及传递至胃和小肠上端的局部和持久给药用于治疗一些特定的情况的药物。Most of the compounds absorb poorly at the back end of the intestine, causing the preparation to be released and absorbed into the colon (usually considered to be 4-6 hours) after the patient takes the preparation, and the preparation cannot be effectively released and absorbed. It is impossible to ensure the effective maintenance of blood concentration 6 hours after taking the medicine by means of ordinary sustained release. The oral gastric retention preparation prolongs the residence time of the drug at the upper end of the gastrointestinal tract, and even if the drug is poorly absorbed at the rear end of the intestinal tract, the drug can be effectively released and absorbed after 6 hours of administration. The dosing interval and dose increase patient compliance. The gastric floating preparation is one of the ways of gastric retention, which increases the residence time of the preparation in the stomach. It has been absorbed in the upper part of the gastrointestinal tract but has little solubility or is easily degraded in an alkaline environment, and is delivered to the stomach. Topical and long-lasting administration of the upper end of the small intestine for the treatment of certain specific conditions.
目前,已经现有大量的现有技术公开了胃漂浮制剂的可实现方式,例如,CN103037850A公开了一类细长型的胃内滞留胶囊,试验表明其出可延长胃滞留时间,然而这样的设计存在胃阻塞或体系永久滞留的危险,故其实际价值很小。为实现更合理的药效,已有大量的药物被制成了速释与控释相结合的胃漂浮给药系统,但是多为双层片或者胶囊,例如尹莉芳等人公开了一种胃漂浮的双层片,活性成分为吡格列酮及二甲双胍,其中速释成分为吡格列酮,控释成分为二甲双胍,该双层片通过使用加入可以产生二氧化碳的碳酸钠以及低密度的漂浮助剂硬脂醇,来达到漂浮的效果,其中最优选的制剂可以在测试溶剂中漂浮至少24h(International Journal of Pharmaceutics 476(2014)223–231)。但是,单一片剂存在存在漂浮能力差、起漂时间长、个体差异大等各种不足。印度专利申请IN2009DE00792A公开了一种双颗粒的胃内给药系统,含有氧氟沙星的速释颗粒及胃漂浮控释颗粒,其中控释颗粒包括疏水性材料和亲水性材料。At present, a large number of prior art has disclosed a achievable manner of gastric floating preparations. For example, CN103037850A discloses a type of elongated intragastric retention capsule, which has been shown to prolong gastric retention time, however, such a design There is a risk of gastric obstruction or permanent retention of the system, so its actual value is small. In order to achieve a more reasonable drug effect, a large number of drugs have been made into a gastric floating drug delivery system combining immediate release and controlled release, but most of them are double-layer tablets or capsules. For example, Yin Lifang et al. disclose a gastric floating system. The bilayer tablet has active ingredients of pioglitazone and metformin, wherein the immediate release component is pioglitazone and the controlled release component is metformin. The bilayer tablet is obtained by adding sodium carbonate which can generate carbon dioxide and a low density floating aid stearyl alcohol. The effect of floating is achieved, with the most preferred formulation being able to float in the test solvent for at least 24 h (International Journal of Pharmaceutics 476 (2014) 223-231). However, single tablets have various disadvantages such as poor floating ability, long drift time, and large individual differences. Indian Patent Application No. 200900/00792 A discloses a dual particle intragastric delivery system comprising immediate release particles of ofloxacin and gastric floating controlled release particles, wherein the controlled release particles comprise a hydrophobic material and a hydrophilic material.
热熔挤出(HME)是通过旋转螺杆将原材料通过模具在高温下泵送成均匀形状的产品的过程。HME具有优于其他药物处理技术的许多优点,在挤出过程中的熔融聚合物可用作热粘合剂,并在冷却和固化时用作药物贮库和/或药物释放阻滞剂。由于该方法不需要溶剂和水,从而减少加工步骤的数量并消除耗时的干燥步骤。基质材料可以被集合成独立于压缩特性的较大单元。旋转螺杆施加的强烈的混合和搅拌引起悬浮颗粒在熔融聚合物中的聚集,使得分散更均匀。Hot melt extrusion (HME) is the process of pumping raw materials through a mold through a mold at a high temperature to a uniform shape product. HME has many advantages over other drug treatment techniques in that the molten polymer can be used as a thermal adhesive during extrusion and as a drug depot and/or drug release blocker upon cooling and solidification. Since the process does not require solvent and water, the number of processing steps is reduced and the time consuming drying step is eliminated. The matrix material can be assembled into larger units that are independent of the compression characteristics. The intense mixing and agitation exerted by the rotating screw causes the agglomeration of suspended particles in the molten polymer to make the dispersion more uniform.
近年来,热熔挤出技术已被尝试用于控释胃漂浮制剂的制备中,Nakamichi等人公开了采用双螺杆挤出机制备的尼卡地平盐酸盐的漂浮制剂,热熔挤出的多聚物材料为醋酸羟丙甲基纤维素琥珀酸酯(HPMCAS),研究中发现,仅使用药物和高聚物并不能得到松胀的挤出物,必须加入第三中物质即二水磷酸钙,当二水磷酸钙的用量为8%时,在胃液中可漂浮6h(International Journal of Pharmace-Utics 218(2001)103–112)。Nakamichi推测了二水合磷酸钙的作用,当药物与高聚物的熔融物在机简内时,受到螺杆的高压作用,从机头挤出的瞬时,由高压区进入了常压区,根据克劳修斯一克拉珀龙方程,熔体的沸点将有下降的趋势,这时,固态的二水合磷酸钙相当于沸石,在熔体中引入了气化中心,使挤出物在瞬间产生了大量气泡。随着温度的快速降低,气泡又立即固化,得到松胀物。In recent years, hot melt extrusion technology has been tried in the preparation of controlled release gastric floating preparations, and Nakamichi et al. disclose a floating preparation of nicardipine hydrochloride prepared by a twin-screw extruder, which is hot melt extruded. The polymer material was hydroxypropylmethylcellulose acetate succinate (HPMCAS). It was found that only the use of drugs and polymers did not result in a loose extrudate, and the third intermediate substance, dihydrate phosphoric acid, must be added. Calcium, when the amount of calcium phosphate dihydrate is 8%, floats in gastric juice for 6 hours (International Journal of Pharmace-Utics 218 (2001) 103-112). Nakamichi speculated that the action of calcium phosphate dihydrate, when the melt of the drug and the polymer is in the machine, is subjected to the high pressure of the screw, and the moment of extrusion from the machine head enters the atmospheric zone from the high pressure zone, according to The Lausius-Clapperon equation, the boiling point of the melt will have a downward trend. At this time, the solid calcium phosphate dihydrate is equivalent to zeolite, and a gasification center is introduced into the melt, so that the extrudate is instantaneously produced. A lot of bubbles. As the temperature rapidly decreases, the bubbles solidify immediately, giving a loose material.
US2016113906A公开了一种热熔挤出的组合物,通过向热熔挤出的组合物中加入极性的有机溶剂,从而使得活性成分的分解减少,增加了活性成分与聚合物之间的混溶性,降低了热熔挤出的操作温度温度,减少了扭矩。Nakamichi等人考察了水分对于通过双螺杆热熔挤出机制备的固体分散体的影响,试验结果证明水的加入会降低物料的流动温度(Tfb),证明物料可以在低于熔点的温度下被挤出(International Journal of Pharmaceutics 241(2002)203–211)。US2016113906A discloses a hot melt extruded composition which, by adding a polar organic solvent to a hot melt extruded composition, reduces the decomposition of the active ingredient and increases the miscibility between the active ingredient and the polymer. Reduces the operating temperature and temperature of the hot melt extrusion and reduces the torque. Nakamichi et al. examined the effect of moisture on solid dispersions prepared by twin-screw hot melt extruders. The results of the tests demonstrate that the addition of water reduces the flow temperature (Tfb) of the material, demonstrating that the material can be at temperatures below the melting point. Extrusion (International Journal of Pharmaceutics 241 (2002) 203-211).
Padma V.Devarajan等人公开了一种通过热熔挤出方式制备的美托洛尔琥珀酸盐的胃漂浮控释多颗粒制剂,优化了热熔挤出的材料尤特奇RSPO
Figure PCTCN2018091103-appb-000001
聚氧化乙烯(PEO)、羟丙甲基纤维素(HPMC)之间的配比来平衡漂浮能力及控释能力,气体的产生使用碳酸钠(International Journal of Pharmaceutics 491(2015)345–351)。
Padma V. Devarajan et al. disclose a gastric floating controlled release multiparticulate formulation of metoprolol succinate prepared by hot melt extrusion to optimize the hot melt extruded material Eudragit RSPO
Figure PCTCN2018091103-appb-000001
The ratio between polyoxyethylene (PEO) and hydroxypropylmethylcellulose (HPMC) is used to balance the floating capacity and the controlled release ability, and the production of gas uses sodium carbonate (International Journal of Pharmaceutics 491 (2015) 345-351).
Mamoru Fukuda等人公开了一种采用热熔挤出的方法制备得到的胃滞留漂浮片,采用尤特奇RSPO(
Figure PCTCN2018091103-appb-000002
RS PO)和或尤特奇EPO(
Figure PCTCN2018091103-appb-000003
E PO.)基质材料,考察了碳酸钠对组合物的理化性质的影(Journal of Controlled Release 115(2006)121–129)。
Mamoru Fukuda et al. disclose a gastric retention floating sheet prepared by hot melt extrusion using Eudragit RSPO (
Figure PCTCN2018091103-appb-000002
RS PO) and or Eudragit EPO (
Figure PCTCN2018091103-appb-000003
E PO.) Matrix material, the effect of sodium carbonate on the physicochemical properties of the composition was examined (Journal of Controlled Release 115 (2006) 121-129).
Michael A.Repka等公开了以尤特奇RSPO
Figure PCTCN2018091103-appb-000004
或羟丙甲基纤维素 K15M(HPMC K15M)为基质材料,采用热熔挤出过程中加入乙醇的操作方法制备得到的胃漂浮微丸(European Journal of Pharmaceutics and Biopharm-
Michael A. Repka et al.
Figure PCTCN2018091103-appb-000004
Or hydroxypropylmethylcellulose K15M (HPMC K15M) as a matrix material, using the method of adding ethanol in the hot melt extrusion process to prepare gastric floating pellets (European Journal of Pharmaceutics and Biopharm-
Aceutics 98(2016)108–121)。Michael A.Repka等人公开了一种含有通过热熔挤出法制备得到的固体分散体的具有双重作用机制的胃内治疗给药系统,该给药系统以非洛地平作为有效成分,羟丙基纤维素基羟甲基纤维素做为基质材料,通过漂浮剂粘附的方式,使得药物在胃内的滞留时间更长(European Journal of Pharmaceutical Sciences 102(2017)71–84),然而,这个剂型固有的危险是药物在食道粘附可能会引起损伤。Aceutics 98 (2016) 108–121). Michael A. Repka et al. disclose a dual-effect intragastric therapeutic delivery system comprising a solid dispersion prepared by hot melt extrusion using felodipine as an active ingredient, hydroxypropyl Cellulose-based hydroxymethylcellulose is used as a matrix material, and the residence time of the drug in the stomach is made longer by the adhesion of the floating agent (European Journal of Pharmaceutical Sciences 102 (2017) 71-84), however, this The inherent danger of the dosage form is that adhesion of the drug to the esophagus may cause damage.
由于热熔挤出技术及胃漂浮制剂均体现出不可替代的优势,且含有速释及控释组分的控释制剂在药效上的优越性有目共睹,因此,综合多种技术,开发出新型的解决各种技术壁垒的制剂,对于制药领域而言重要性不言而喻。Because of the irreplaceable advantages of hot melt extrusion technology and gastric floating preparations, and the superiority of the controlled release preparations containing immediate release and controlled release components in terms of efficacy, it is obvious that a variety of technologies have been developed to develop new types. The formulation of various technical barriers is of great importance to the pharmaceutical industry.
发明内容Summary of the invention
本发明提供了一种采用热熔挤出制备的控释药物组合物,该组合物有效延长了在胃肠道中前端停留时间,将胃肠道有效吸收时间提高至10小时以上,从而有效减少用药次数,增加患者服药的依从性。The invention provides a controlled release pharmaceutical composition prepared by hot melt extrusion, which effectively prolongs the residence time in the gastrointestinal tract and increases the effective absorption time of the gastrointestinal tract to more than 10 hours, thereby effectively reducing the dosage. The number of times increases the compliance of patients taking medication.
本发明提供了一种控释药物组合物,包含:a)含有活性药物的速释组分,b)含有活性药物的延迟释放漂浮组分,其特征在于所述延迟释放漂浮组分通过热熔挤出的过程制备。The present invention provides a controlled release pharmaceutical composition comprising: a) an immediate release component comprising an active drug, b) a delayed release floating component comprising an active drug, characterized in that said delayed release floating component is passed through a heat fusion The extrusion process is prepared.
本发明提供的控释药物组合物,其特征在于所述的延迟释放漂浮组分含有至少一种肠溶性聚合物。本发明所述的含有肠溶性聚合物的延迟释放药物组分在pH≥5.5的条件下释放药物。The controlled release pharmaceutical composition of the present invention is characterized in that the delayed release floating component contains at least one enteric polymer. The delayed release drug component containing the enteric polymer of the present invention releases the drug at a pH of ≥ 5.5.
本发明提供的控释药物组合物,其特征在于所述的肠溶性聚合物选自聚乙烯醇乙酸苯二甲酸酯、邻苯二甲酸乙酸纤维素、1,2,4-苯三甲酸乙酸纤维素、邻苯二甲酸羟丙基甲基纤维素、1,2,4-苯三甲酸羟丙基甲基纤维素、琥珀酸乙酸纤维素、醋酸羟丙甲纤维素琥珀酸酯、醋酸羟丙基甲基纤维素酞酸酯、甲基丙烯酸-丙烯酸乙酯共聚物、甲基乙烯基醚-马来酸酐共聚物、甲基丙烯酸-丙烯酸乙酯共聚物水分散体、甲基丙烯酸-甲基丙烯酸甲酯共聚物、丙烯酸乙酯-甲基丙烯酸甲酯-甲基丙烯酸氯化三甲胺基乙酯共聚物、聚乙酸乙烯酯、乙基纤维素、聚醋酸乙烯酯与聚乙烯吡咯烷酮K30混合物,优选醋酸羟丙甲纤维素琥珀酸酯、甲基丙烯酸-甲基丙烯酸甲酯共聚物、甲基丙烯酸-丙烯酸乙酯共聚物、邻苯二甲酸羟丙基甲基纤维素。The controlled release pharmaceutical composition provided by the present invention is characterized in that the enteric polymer is selected from the group consisting of polyvinyl alcohol acetate phthalate, cellulose acetate phthalate, and 1,2,4-benzenetricarboxylic acid acetic acid. Cellulose, hydroxypropyl methylcellulose phthalate, hydroxypropyl methylcellulose 1,2,4-benzenetricarboxylate, cellulose acetate succinate, hypromellose acetate succinate, hydroxyacetate Propylmethylcellulose phthalate, methacrylic acid-ethyl acrylate copolymer, methyl vinyl ether-maleic anhydride copolymer, methacrylic acid-ethyl acrylate copolymer aqueous dispersion, methacrylic acid-A Methyl methacrylate copolymer, ethyl acrylate-methyl methacrylate-trimethylaminoethyl methacrylate copolymer, polyvinyl acetate, ethyl cellulose, polyvinyl acetate and polyvinylpyrrolidone K30 mixture Preferably, hypromellose acetate succinate, methacrylic acid-methyl methacrylate copolymer, methacrylic acid-ethyl acrylate copolymer, hydroxypropyl methylcellulose phthalate.
在一些实施方案中,甲基丙烯酸-丙烯酸乙酯共聚物为1:1共聚物,对应市售Eudragit  l 100-55或者Kollicoat MAE100P。In some embodiments, the methacrylic acid-ethyl acrylate copolymer is a 1:1 copolymer corresponding to commercially available Eudragit 100-55 or Kollicoat MAE 100P.
在一些实施方案中,甲基乙烯基醚-马来酸酐共聚物对应市售
Figure PCTCN2018091103-appb-000005
系列。
In some embodiments, the methyl vinyl ether-maleic anhydride copolymer is commercially available.
Figure PCTCN2018091103-appb-000005
series.
在一些实施方案中,甲基丙烯酸-甲基丙烯酸甲酯共聚物为1:1或者1:2共聚物,分别对应Eudragit L100以及Eudragit S100。In some embodiments, the methacrylic acid-methyl methacrylate copolymer is a 1:1 or 1:2 copolymer corresponding to Eudragit L100 and Eudragit S100, respectively.
在一些实施方案中,聚醋酸乙烯酯与聚乙烯吡咯烷酮K30混合物为Kollidon SR。In some embodiments, the mixture of polyvinyl acetate and polyvinylpyrrolidone K30 is Kollidon SR.
在一些实施方案中,本发明中所述肠溶性聚合物是Eudragit聚合物,例如Eudragit L,Eudragit S或EudragitL 100-55。In some embodiments, the enteric polymer described herein is an Eudragit polymer, such as Eudragit L, Eudragit S or Eudragit L 100-55.
在一些实施方案中,本发明中所述的肠溶聚合物是乙酸琥珀酸羟丙基甲基纤维素(HPMCAS),现有技术US4226981B、CN104208713A及CN103153343A中公开的乙酸琥珀酸羟丙基甲基纤维素包含在本申请的范围内。In some embodiments, the enteric polymer described in the present invention is hydroxypropyl methylcellulose acetate succinate (HPMCAS), hydroxypropyl methyl acetate succinate disclosed in the prior art US 4,266,981 B, CN 104208713 A, and CN 103153343 A. Cellulose is included within the scope of this application.
Shin-Etsu Chemical Co.,Ltd.(日本东京)销售的HPMCAS分三种等级,其具有取代基水平不同的组合,以在各种不同pH水平下提供肠溶保护。AS-LF和AS-LG级(“F”表示细且“G”表示颗粒状)在最高5.5的pH下提供肠溶保护。AS-MF和AS-MG级在最高6.0的pH下提供肠溶保护,而AS-HF和AS-HG级在最高6.8的pH下提供肠溶保护。HPMCAS sold by Shin-Etsu Chemical Co., Ltd. (Tokyo, Japan) is classified into three grades having different combinations of substituent levels to provide enteric protection at various pH levels. AS-LF and AS-LG grades ("F" means fine and "G" means granules) provide enteric protection at a pH of up to 5.5. The AS-MF and AS-MG grades provide enteric protection at pH values up to 6.0, while the AS-HF and AS-HG grades provide enteric protection at pHs up to 6.8.
本发明提供的控释药物组合物特征在于所述延迟释放漂浮组分中活性药物与肠溶性聚合物比例选自1:0.1-1:100,优选1:0.1-1:50,更优选1:1-1:25。The controlled release pharmaceutical composition provided by the present invention is characterized in that the ratio of the active drug to the enteric polymer in the delayed release floating component is selected from 1:0.1 to 1:100, preferably from 1:0.1 to 1:50, more preferably 1: 1-1:25.
本发明提供的控释药物组合物,所述的热熔挤出方法任选溶剂参与热熔挤出过程,即在某些方案中,加入溶剂,在另一些方案中不加入溶剂,本发明中所述溶剂参与是指为发明需要,在热熔挤出前或者热熔挤出过程中加入溶剂。The controlled release pharmaceutical composition provided by the present invention, wherein the hot melt extrusion method optionally participates in a hot melt extrusion process, that is, in some embodiments, a solvent is added, and in other embodiments, a solvent is not added, in the present invention The participation of the solvent means that the solvent is added before the hot melt extrusion or during the hot melt extrusion process for the needs of the invention.
本发明提供的控释药物组合物在制备过程中若加入溶剂,则所述溶剂只需要满足在热熔挤出过程结束后可以被挥发即可,优选的,本发明将溶剂的沸点限定为30-110℃。In the controlled release pharmaceutical composition provided by the present invention, if a solvent is added during the preparation, the solvent only needs to be able to be volatilized after the end of the hot melt extrusion process. Preferably, the present invention limits the boiling point of the solvent to 30. -110 ° C.
本发明提供的控释药物组合物,其特征在于所述溶剂选自水、甲醇、乙醇、异丙醇、丙酮、戊烷、己烷、庚烷、环己烷、二氯甲烷、四氢呋喃的至少一种,优选水和乙醇。The controlled release pharmaceutical composition provided by the present invention is characterized in that the solvent is at least selected from the group consisting of water, methanol, ethanol, isopropanol, acetone, pentane, hexane, heptane, cyclohexane, dichloromethane, tetrahydrofuran. One is preferably water and ethanol.
本发明提供一种控释药物组合物,当有溶剂参与热熔挤出过程时,控释药物组合物中的延迟释放漂浮组分密度为0.1-1.0g/cm3,优选0.2-0.8g/cm3,最优选0.3-0.7g/cm3,在电镜下显示为多孔状,并且可以在pH5.0的FaSSGF的溶液中立即起漂并维持漂浮时间大于24h。The present invention provides a controlled release pharmaceutical composition having a density of delayed release floating components in a controlled release pharmaceutical composition of from 0.1 to 1.0 g/cm3, preferably from 0.2 to 0.8 g/cm3, when a solvent is involved in the hot melt extrusion process. Most preferably, it is 0.3-0.7 g/cm3, which is porous under electron microscopy, and can be floated immediately in a solution of FaSSGF at pH 5.0 and maintained for a float time of more than 24 h.
本发明提供的控释药物组合物在制备过程中若不加溶剂,含有遇酸产生气体的碱性物质,即本发明中控释药物组合物中碱性物质不是必须的,当含有碱性物质时,所述碱性物质具体为碱金属碳酸盐、碱金属或者碱土金属碳酸氢盐,更具体为碳酸氢钠、碳酸钠、氨基乙酸钠碳酸盐、碳酸氢钾、碳酸镁和碳酸钙。The controlled release pharmaceutical composition provided by the present invention contains an alkaline substance which is exposed to an acid generating gas in the preparation process without adding a solvent, that is, the alkaline substance in the controlled release pharmaceutical composition of the present invention is not essential, and when the alkaline substance is contained The basic substance is specifically an alkali metal carbonate, an alkali metal or an alkaline earth metal hydrogencarbonate, more specifically sodium hydrogencarbonate, sodium carbonate, sodium aminoacetate carbonate, potassium hydrogencarbonate, magnesium carbonate and calcium carbonate. .
本发明提供的控释药物组合物不含二水磷酸钙,Nakamichi(International Journal of Pharmace-Utics 218(2001)103–112),等人将二水磷酸钙加入药物和基质,并通过热熔挤出后,制备得到漂浮剂。The controlled release pharmaceutical composition provided by the present invention does not contain calcium phosphate dihydrate, Nakamichi (International Journal of Pharmace-Utics 218 (2001) 103-112), and others add calcium phosphate dihydrate to the drug and the matrix, and by hot melt extrusion After that, a floatant was prepared.
本发明提供的控释药物组合物,所述延迟释放漂浮组分在300mL的pH5.0的FaSSGF溶出介质中,篮法,37℃,100rpm,5h的累积溶出小于30%,更优选小于20%,最优选小于10%。The controlled release pharmaceutical composition provided by the present invention, the delayed release floating component in a 300 mL of FaSSGF dissolution medium at pH 5.0, the basket method, 37 ° C, 100 rpm, 5 h cumulative dissolution is less than 30%, more preferably less than 20% Most preferably less than 10%.
本发明提供的控释药物组合物,其特征在于延迟释放漂浮组分为多单元形式。The controlled release pharmaceutical composition of the present invention is characterized in that the delayed release floating component is in a multi-unit form.
本发明提供的控释药物组合物,其特征在于所述多单元形式为微片、微丸、颗粒,优选颗粒。The controlled release pharmaceutical composition of the present invention is characterized in that the multi unit form is a microtablet, a pellet, a pellet, preferably a pellet.
本发明提供的控释药物组合物中速释组分可选为微丸、微片、颗粒等多种形式,具体的,当速释组分为微丸时,可含有活性药物和空白丸芯。The immediate release component of the controlled release pharmaceutical composition provided by the invention may be selected from the form of pellets, microtablets, granules and the like. Specifically, when the immediate release component is a pellet, the active drug and the blank pellet core may be contained. .
通常,药物制剂在口服之后大部分情况之下会在3到6h到达结肠,因此,缓释制剂成功的前提是提高胃肠吸收的时间并增加吸收。In general, pharmaceutical preparations reach the colon in most cases after oral administration in 3 to 6 hours. Therefore, the success of the sustained-release preparation is to increase the time of gastrointestinal absorption and increase absorption.
由FDA引入的生物制药分类系统(BCS)已经将药物按照它们的溶解性和肠道通透性进行分类,具体参见“The Biopharmaceutics Classification System(BCS)Guidance”。Jennifer B.Dressman和Christos Reppas在《Oral Drug Absorption:Prediction and Assessment》273页提到在口服给药时具有高可溶性和渗透性的药物(Ⅰ类)通常在整个胃肠道具有好的吸收度,是缓释制剂最优选的药物,这类药物包含在本发明所述的延迟释放漂浮组分的活性药物的范围内。The Biopharmaceutical Classification System (BCS) introduced by the FDA has classified drugs according to their solubility and intestinal permeability, see "The Biopharmaceutics Classification System (BCS) Guidance". Jennifer B. Dressman and Christos Reppas, on page 273 of the Oral Drug Absorption: Prediction and Assessment, mention that drugs that have high solubility and permeability when administered orally (Class I) generally have good absorption throughout the gastrointestinal tract. It is the most preferred drug for the sustained release preparation, and such a drug is included in the range of the active drug of the delayed release floating component of the present invention.
本发明所述的BCS分类中Ⅰ类的药物包括但不限于:帕比司他、Cobimetinib、Patiromer、omarigliptin、安非他酮、胍法辛、文拉法辛盐酸盐、盐酸哌甲酯、磷酸泰地唑胺、氟班色林、eliglustat、阿格列汀、富马酸二甲酯、吡仑帕奈、洛美他派、卢索替尼、氯巴占、dalfampridine、Prolia、决奈达隆盐酸盐、Pralatrexate、lacosamide、fesoterodine fumarate、阿普唑仑、阿米替林盐酸盐、氨氯地平苯磺酸盐、贝那普利、阿莫西林、阿那曲唑、氮卓斯汀、比索洛尔、丁螺环酮、咖啡因、卡比多巴、西替利嗪、磷酸氯喹、扑尔敏、克林霉素、可乐定、环苯扎林、环磷酰胺、去氧孕烯、炔雌醇、地西泮、苯海拉明、多奈哌齐盐酸盐、多沙唑嗪甲磺酸盐、多西环素、恩曲他滨、雌二醇、乙琥胺、非索非那定、非那雄胺、氟康唑、氟胞嘧啶、氟西汀盐酸盐、氟伏沙明甲磺酸盐、丙咪嗪、吲达帕胺、异烟肼、拉米夫定、利多卡因、劳拉西泮、氯沙坦、琥珀酸美托洛尔、美西律、咪达唑仑、米氮平、孟鲁司特钠、炔诺酮、甲基炔诺酮、去甲替林、奥洛他定盐酸盐、奥司他韦、普拉克索、普伐他汀钠、强的松、泼尼松龙、普瑞巴林、普鲁卡因胺盐 酸盐、异丙嗪盐酸盐、普萘洛尔盐酸盐、吡嗪酰胺、吡哆醇盐酸盐、喹那普利盐酸盐、奎尼丁、奎宁盐酸盐、雷米普利、舍曲林、枸橼酸西地那非、索他洛尔、司他夫定、特比萘芬盐酸盐、托特罗定、托拉塞米、曲马朵盐酸盐、曲唑酮、伐尼克兰、齐多夫定、阿法骨化醇、贝前列素、比哌立登、溴苯那敏、溴替唑仑、卡比沙明、克罗米芬、氯米帕明、氯唑西林、地尔硫卓、多拉司琼、吗丁啉、盐酸乙哌立松、依匹斯汀、钙化醇、麦角新碱、麦角胺、乙炔雌二醇、依替唑仑、氟伐他汀、格拉司琼、酮替芬、左旋咪唑、左炔诺孕酮、立马前列素、洛索洛芬、甲氟喹、盐酸美西律、尼卡地平、氯硝柳胺、妥布特罗、甲氧苄啶、曲美布汀、托瑞米芬、特比萘芬、替莫普利、坦索罗辛、舍曲林、盐酸沙格雷酯、沙奎那韦、罗格列酮、利血平、雷米普利、盐酸丙哌维林、异丙嗪、培高利特、帕罗西汀。Class I drugs in the BCS classification of the present invention include, but are not limited to, pabitatin, Cobimetinib, Patiromer, omarigliptin, bupropion, guanfacine, venlafaxine hydrochloride, methylphenidate hydrochloride, Tetrazolamide, flurbanin, eliglustat, alogliptin, dimethyl fumarate, pyrenoprene, lometanide, rosobinib, clozaban, dalfampridine, Prolia, drone Dalong hydrochloride, Pralatrexate, lacosamide, fesoterodine fumarate, alprazolam, amitriptyline hydrochloride, amlodipine besylate, benazepril, amoxicillin, anastrozole, azastroz Ting, bisoprolol, buspirone, caffeine, carbidopa, cetirizine, chloroquine phosphate, chlorpheniramine, clindamycin, clonidine, cyclobenzaprine, cyclophosphamide, deoxygenation Pregnene, ethinyl estradiol, diazepam, diphenhydramine, donepezil hydrochloride, doxazosin mesylate, doxycycline, emtricitabine, estradiol, ethosylamine, fensamine Phenazepine, finasteride, fluconazole, flucytosine, fluoxetine hydrochloride, fluvoxamine mesylate, imipramine, guanidine Pamine, isoniazid, lamivudine, lidocaine, lorazepam, losartan, metoprolol succinate, mexiletine, midazolam, mirtazapine, montelukast sodium , norethisterone, norgestrel, nortriptyline, olopatadine hydrochloride, oseltamivir, pramipexole, pravastatin sodium, prednisone, prednisolone, pregabalin , procainamide hydrochloride, promethazine hydrochloride, propranolol hydrochloride, pyrazinamide, pyridoxine hydrochloride, quinapril hydrochloride, quinidine, quinine Hydrochloride, ramipril, sertraline, sildenafil citrate, sotalol, stavudine, terbinafine hydrochloride, tolterodine, torasemide, ko Malone hydrochloride, trazodone, varenicline, zidovudine, alfacalcidol, beraprost, biperiden, brompheniramine, bromozolam, carbifamine, clomiphene , clomipramine, cloxacillin, diltiazem, dolasetron, morphine, eperisone hydrochloride, epilistin, calciferol, ergometrine, ergotamine, ethinyl estradiol, etidazolam , fluvastatin, granisetron, Tetfen, levamisole, levonorgestrel, erimaprost, loxoprofen, mefloquine, mexiletine hydrochloride, nicardipine, niclosamide, tobrexol, trimethoprim, koji Mebutin, toremifene, terbinafine, temocapril, tamsulosin, sertraline, sarpogrelate hydrochloride, saquinavir, rosiglitazone, reserpine, remept Lee, propiverine hydrochloride, promethazine, pergolide, paroxetine.
Jennifer B.Dressman和Christos Reppas在《Oral Drug Absorption:Prediction and Assessment》272-274页指出由于渗透性和溶解性的问题,BCS分类中的Ⅱ至Ⅳ类的药物表现出结肠吸收差或者溶解度差,不适合制备成缓释制剂,本发明的组合物由于使用了热熔挤出技术及胃漂浮技术,特别是采用了肠溶性聚合,有效的延长了该类药物在胃肠道的滞留时间,提高了药物在小肠的吸收率,针对该类的药物体现出了更优的效果。Jennifer B. Dressman and Christos Reppas on page 272-274 of Oral Drug Absorption: Prediction and Assessment indicate that Class II to IV drugs in the BCS classification show poor colonic absorption or poor solubility due to problems with permeability and solubility. Unsuitable for preparation into a sustained-release preparation, the composition of the present invention effectively uses the enteric polymerization to effectively prolong the residence time of the drug in the gastrointestinal tract due to the use of hot melt extrusion technology and gastric floating technology, especially the use of enteric polymerization. The absorption rate of the drug in the small intestine shows a better effect for the drug of this kind.
本发明所述的BCS分类属于Ⅱ至Ⅳ类的药物包括但不限于:非布司他、ixazomib、Alectinib、Erismodegib、凡德他尼、阿瑞匹坦、硫酸沃拉帕沙、阿司匹林、二甲双胍、恩格列净、利格列汀、纳曲酮、dasabuvir、索非布韦、安非他明、依曲韦林、依维莫司、伊曲康唑、维罗非尼、特拉匹韦、他克莫司、泊沙康唑、依伐卡托、雷迪帕韦、Suvorexant、Ombitasvir、paritaprevir、daclatasvir、卡利拉嗪、brexpiprazole、奥培米芬、左乙拉西坦、ivacaftor、eluxadoline、lumacaftor、ivacaftor、艾曲泊帕、尼达尼布、美洛昔康、吗啡、马西替坦、度他雄胺、阿比特龙、lumacaftor、达格列净、他司美琼、依鲁替尼、帕拉米韦、奥拉帕尼、依帕列净、idelalisib、贝利司他、色瑞替尼、阿普斯特、泊马度胺、奥培米芬、卡格列净、甲磺酸达拉非尼、曲美替尼、dolutegravir、vortioxetine、bazedoxifene、simeprevir、阿西替尼、Vismodegib、阿伐那非、氯卡色林、米拉贝隆、博舒替尼、特立氟胺、Regorafenib、托法替尼、Cabozantinib、帕纳替尼、阿哌沙班、Bedaquiline、Crofelemer、波塞普韦、特拉普韦、贝拉赛普、维拉芬尼、克唑替尼、罗氟司特、维拉唑酮、阿梓沙坦、加巴喷丁、范德他尼、那格列汀、利匹韦林、非达霉素、依佐加滨、醋酸艾替班特、利伐沙班、替卡格雷、polidocanol、carglumic acid、替莫瑞林、vemurafenib、cabazitaxel、达比加群酯、依维莫司、托伐普坦、prasugrel、saxagliptin、telavancin、pazopanib、silodosin、rufinamide、艾曲波帕、乙酰唑胺、对乙酰氨基酚、阿昔洛韦、阿托伐他汀、阿托伐他汀 钙、安普那韦、阿立哌唑、阿替洛尔、氯胺酮、阿托喹酮、咪唑硫嘌呤、阿奇霉素、布地奈德、骨化三醇、异丙基甲丁双脲、头孢地尼、头孢克肟、乙酸头孢呋辛、塞来昔布、头孢氨苄、氯噻嗪、克拉霉素、氯吡格雷硫酸氢盐、克霉唑、倍他米松、二氨二苯酚、双氯芬酸钠、双环胺、抵达诺新、曲大麻酚、度洛西汀、度他雄胺、依托度酸、依泽替米贝、辛伐他汀、非尔氨酯、非诺贝特、氟卡尼、膦沙那韦、呋喃苯胺酸、二甲苯氧庚酸、格列美脲、格列本脲、灰黄霉素、布洛芬、羟化氯喹、羟嗪、吲哚美辛、厄贝沙坦、异烟肼、依拉地平、酮康唑、拉莫三嗪、兰索拉唑、拉坦前列素、利奈唑胺、洛派丁胺、氯碳头孢、氯雷他定、洛伐他汀、甲苯咪唑、氯苯甲嗪、巯嘌呤、氨水杨酸、美他沙酮、苯哌啶醋酸甲酯、甲基强的松龙、莫达非尼、麦考酚酸、麦考酚酸酯、纳布美通、萘普生、硝苯地平、奥美拉唑、卡马西平、盐酸羟考酮、非那吡啶、苯妥英钠、吡格列酮盐酸盐、吡罗昔康、去氧苯巴比妥、丙氯拉嗪、黄体酮、乙胺嘧啶、奎硫平、雷洛昔芬盐酸盐、利福布汀、利福平、利培酮、螺内酯、磺胺甲恶唑、他达拉非、替米沙坦、替拉那韦、缬沙坦、伐地那非、齐拉西酮、硫酸阿巴卡韦、可待因、沙丁胺醇、阿仑膦酸钠、别嘌醇、克拉维酸钾、苯甲托品、比马前列素、丁苯诺啡、纳洛酮、卡托普利、左旋多巴、头孢克肟、头孢羟氨苄、西替利嗪盐酸盐、环丙沙星、秋水仙碱、麦角钙化醇、法莫替丁、伪麻黄碱、叶酸、加巴喷丁、肼苯哒嗪、氢氯噻嗪、沙丁胺醇、左西替利、左氧氟沙星、左甲状腺素钠、赖诺普利、氨甲喋呤、甲基多巴、纳多洛尔、制霉菌素、泮托拉唑、磷酸伯氨喹、吡嗪酰胺、雷尼替丁盐酸盐、利巴韦林、利塞膦酸钠、索利那新、安体舒通、舒马曲普坦琥珀酸盐、特拉唑嗪、四环素、硫胺素、托吡酯、伐昔洛韦盐酸盐、缬更昔洛韦、阿卡波糖、醋氯芬酸、乙酰唑胺、乙酰肉毒碱、阿苯达唑、烯丙柳胺醇、阿米洛利、阿托品、硫唑嘌呤、阿奇霉素、贝尼地平、苄丝肼、苄硝唑、比卡鲁胺、比沙可啶、卡麦角林、坎地沙坦、卡培他滨、卡维地洛、头孢托仑、头孢美唑、头孢替安、头孢泊肟、头孢他啶、头孢呋辛酯、塞来考昔、氯霉素、氯丙嗪、西拉普利、西洛他唑、西咪替丁、西酞普兰、氯苯吩嗪、环孢素、环丙孕酮、氨苯砜、乙胺嗪、地高辛、二氯尼特、脱氧氟尿苷、强力霉素、依巴斯汀、依法韦仑、依帕司他、普沙坦、红霉素、乙胺丁醇、依泽替米贝、泛昔洛韦、非诺贝特、氟康唑、氟比洛芬、利尿磺胺、呋喃硫胺、吉非替尼、格列齐特、格列吡嗪、灰黄霉素、氟哌啶醇、盐酸羟嗪、布洛芬、伊马替尼、咪达普利、茚地那韦、厄贝沙坦、异烟肼、伊维菌素、酮洛芬、拉莫三嗪、左氧氟沙星、洛匹那韦、乐伐他汀、马尼地平、甲苯咪唑、甲羟孕酮、氨基水杨酸、美他沙酮、甲氨蝶呤、甲基多巴、甲硝唑、莫达非尼、莫沙必利、萘丁美酮、萘啶酸、奈非那韦、新斯的明、奈韦拉平、尼可地尔、烟酰胺、硝呋莫司、尼伐地平、尼美舒利、唑吡 坦、佐米曲普坦、扎托洛芬、华法林、伏格列波糖、维拉帕米、丙戊酸、熊去氧胆酸、曲美他嗪、妥舒沙星、噻氯匹定、茶碱、替普瑞酮、替诺福韦、替加氟、他莫昔芬、他替瑞林、舒他西林、舒必利、柳氮磺胺吡啶、磺胺甲恶唑、磺胺嘧啶、司他夫定、罗红霉素、罗非昔布、利扎曲普坦、利托那韦、利塞膦酸、利福平、利福昔明、瑞巴派特、雷尼替丁、雷贝拉唑、尼扎替丁、炔诺酮、奥氮平、奥洛他定、奥利司他、奥司他韦、奥卡西平、喹硫平、盐酸吡哆醇、溴吡斯、丙基硫氧嘧啶、丙卡特罗、吡喹酮、普鲁司特、苯妥英钠、苯巴比妥、苯甲曲秦、培哚普利、羟考酮、地塞米松、呋塞米。The BCS classification of the present invention belongs to the class II to IV drugs including, but not limited to, febuxostat, ixazomib, Alectinib, Erismodegib, vandetanib, aprepitant, worapsar sulfate, aspirin, metformin, Engliflozin, linagliptin, naltrexone, dasabuvir, sofosbuvir, amphetamine, etravirine, everolimus, itraconazole, vemurafenib, telaprevir , tacrolimus, posaconazole, isikato, redipavir, Suvorexant, Ombitasvir, paritaprevir, daclatasvir, cariprazine, brexpiprazole, omemiprofen, levetiracetam, ivacaftor, eluxadoline , lumacaftor, ivacaftor, atratropa, nidanib, meloxicam, morphine, macitentan, dutasteride, abiraterone, lumacaftor, dagley net, hesiqiong, yilu Tinidil, peramivir, olrapani, empaglifloz, itelalisib, balystatin, ceritinib, apster, pomamide, omemiprofen, calpamin, Dalafenib mesylate, trimetinib, dolutegravir, vortioxetine, bazedoxifene, simeprevir, ar Cetinib, Vismodegib, Avavira, lorcaserin, Mirabelon, Bosutinib, Triflurane, Regorafenib, Tofacitinib, Cabozantinib, Panatinib, Apixaban, Bedaquiline, Crofelemer, Poseprevir, Traverse, Bellasep, Vilafenib, Crizotinib, Roflumilast, Verazodone, Alzartan, Gabapentin, Van derani Nalagliptin, rivivirin, fidarimycin, ezitabine, icatibine acetate, rivaroxaban, ticagrelor, polidocanol, carglumic acid, temoline, vemurafenib, cabazitaxel, Dabigatran etexilate, everolimus, tolvaptan, prasugrel, saxagliptin, telavancin, pazopanib, silodosin, rufinamide, eltrombopag, acetazolamide, acetaminophen, acyclovir, atovava Statins, atorvastatin calcium, amprenavir, aripiprazole, atenolol, ketamine, attorikone, azathioprine, azithromycin, budesonide, calcitriol, isopropyl methacrylate Diurea, cefdinir, cefixime, cefuroxime acetate, celecoxib, cephalosporin Benzyl, chlorothiazide, clarithromycin, clopidogrel hydrogen sulphate, clotrimazole, betamethasone, diaminodiphenol, diclofenac sodium, bicyclic amine, arrived in Nuoxin, cannabinol, duloxetine, degree Otamin, etodolac, ezetimibe, simvastatin, felamine, fenofibrate, flecainide, phosphaviravir, furosemide, xyloxyheptanoic acid, glime Urea, glibenclamide, griseofulvin, ibuprofen, hydroxychloroquine, hydroxyzine, indomethacin, irbesartan, isoniazid, iraradipine, ketoconazole, lamotrigine, Lansoprazole, latanoprost, linezolid, loperamide, chlorocarbon cephalosporin, loratadine, lovastatin, mebendazole, meclizine, guanidine, salicylic acid, metha Ketone, piperidine acetate methyl ester, methylprednisolone, modafinil, mycophenolic acid, mycophenolate mofetil, nabumetone, naproxen, nifedipine, omeprazole, Carbamazepine, oxycodone hydrochloride, phenazopyridine, phenytoin, pioglitazone hydrochloride, piroxicam, deoxyphenobarbital, prochlorperazine, progesterone, pyrimethamine, Quetiapine, raloxifene hydrochloride, rifabutin, rifampicin, risperidone, spironolactone, sulfamethoxazole, tadalafil, telmisartan, telavanavir, valsartan , vardenafil, ziprasidone, abacavir sulfate, codeine, albuterol, alendronate, allopurinol, potassium clavulanate, benzotropine, bimatoprost, butylbenzene Normaine, naloxone, captopril, levodopa, cefixime, cefadroxil, cetirizine hydrochloride, ciprofloxacin, colchicine, ergocalciferol, famotidine, Pseudoephedrine, folic acid, gabapentin, hydralazine, hydrochlorothiazide, salbutamol, levocetirizine, levofloxacin, levothyroxine sodium, lisinopril, methotrexate, methyldopa, nadolol, nystatin, Latrazole, primaquine phosphate, pyrazinamide, ranitidine hydrochloride, ribavirin, risedronate sodium, solifenacin, spironolactone, sumatriptan succinate, Terazosin, tetracycline, thiamine, topiramate, valacyclovir hydrochloride, valganciclovir, acarbose, aceclofenac, Acylzolamine, acetylcarnitine, albendazole, allenamide, amiloride, atropine, azathioprine, azithromycin, benidipine, benserazide, benznidazole, bicalutamide, Bisacodidine, cabergoline, candesartan, capecitabine, carvedilol, cefditoren, cefmetazole, cefotiam, cefpodoxime, ceftazidime, cefuroxime axetil, celecoxib , chloramphenicol, chlorpromazine, cilazapril, cilostazol, cimetidine, citalopram, chlorpheniramine, cyclosporine, cyproterone, dapsone, ethamazine, Digoxin, diclofen, deoxyfluorouridine, doxycycline, ebastine, efavirenz, epalrestat, valsartan, erythromycin, ethambutol, ezetimibe , famciclovir, fenofibrate, fluconazole, flurbiprofen, diurea, furosemide, gefitinib, gliclazide, glipizide, griseofulvin, haloperidol, hydrochloric acid Hydroxyzine, ibuprofen, imatinib, midazolam, indinavir, irbesartan, isoniazid, ivermectin, ketoprofen, lamotrigine, levofloxacin, lopi Wei, lovastatin, manidipine, mebendazole, medroxyprogesterone, aminosalicylic acid, metaxalone, methotrexate, methyldopa, metronidazole, modafinil, mosapride , nabumetone, nalidixic acid, nelfinavir, neostigmine, nevirapine, nicorandil, nicotinamide, nifurolimus, nilvadipine, nimesulide, zolpidem, zo Mitreloptan, zaltoprofen, warfarin, voglibose, verapamil, valproic acid, ursodeoxycholic acid, trimetazidine, tosufloxacin, ticlopidine, Theophylline, teprenone, tenofovir, tegafur, tamoxifen, statin, sultasis, sulpiride, sulfasalazine, sulfamethoxazole, sulfadiazine, stavudine , roxithromycin, rofecoxib, rizatriptan, ritonavir, risedronate, rifampicin, rifaximin, rebamipide, ranitidine, rabeprazole , nizatidine, norethisterone, olanzapine, olopatadine, orlistat, oseltamivir, oxcarbazepine, quetiapine, pyridoxine hydrochloride, bromide, propylthio Pyrimidine, Procaterol, Praziquantel, Montelukast, phenytoin, phenobarbital, phendimetrazine, perindopril, oxycodone, dexamethasone, furosemide.
本发明提供的控释药物组合物,其特征在于所述延迟释放漂浮组分还可包含至少一种塑化剂,所述塑化剂选自枸橼酸三乙酯、枸橼酸三丁酯、聚乙二醇、邻苯二甲酸三乙酯、邻苯二甲酸三丁酯、癸二酸二丁酯、癸二酸二乙酯、硬脂酸甘油酯、丁二酸二乙酯、丙二醇、蓖麻油和三乙酸甘油酯,优选枸橼酸三乙酯,所述增塑剂的含量为0.01%-50%,优选0.1-30%,最优选2.5%-15%(质量百分比,以固体组分的总质量为100计算)。The controlled release pharmaceutical composition provided by the present invention is characterized in that the delayed release floating component further comprises at least one plasticizer selected from the group consisting of triethyl citrate and tributyl citrate. , polyethylene glycol, triethyl phthalate, tributyl phthalate, dibutyl sebacate, diethyl sebacate, glyceryl stearate, diethyl succinate, propylene glycol , castor oil and triacetin, preferably triethyl citrate, the plasticizer is present in an amount of from 0.01% to 50%, preferably from 0.1% to 30%, most preferably from 2.5% to 15% (% by mass, by solids) The total mass of the components is calculated as 100).
在一些实施方案中,本发明提供的控释药物组合物中速释组分和/或控释漂浮组分还包含至少一种药学上可接受的其他赋形剂,药学上常用的赋形剂包括但不限于填充剂、润滑剂、助流剂、粘合剂、崩解剂。In some embodiments, the immediate release component and/or the controlled release floating component of the controlled release pharmaceutical composition provided herein further comprises at least one pharmaceutically acceptable additional excipient, a pharmaceutically acceptable excipient These include, but are not limited to, fillers, lubricants, glidants, binders, disintegrants.
如本领域技术人员所熟知的,常规地将药物赋形剂混入固体剂型中从而使操作过程容易进行以及改善剂型的性能。常见的赋形剂包括稀释剂或填充剂、润滑剂、助流剂、粘合剂、崩解剂等。其中稀释剂或填充剂以便增加单个剂量的重量至适于片剂压缩的大小。适当的稀释剂包括糖粉、磷酸钙、硫酸钙、微晶纤维素、乳糖、甘露醇、高岭土、氯化钠、干燥淀粉、山梨醇等。As is well known to those skilled in the art, pharmaceutical excipients are conventionally incorporated into solid dosage forms to facilitate ease of handling and to improve the performance of the dosage form. Common excipients include diluents or fillers, lubricants, glidants, binders, disintegrants, and the like. Wherein a diluent or filler is added to increase the weight of the individual dose to a size suitable for tablet compression. Suitable diluents include powdered sugar, calcium phosphate, calcium sulfate, microcrystalline cellulose, lactose, mannitol, kaolin, sodium chloride, dried starch, sorbitol, and the like.
润滑剂降低了在压缩和排出期间颗粒和模具壁之间的摩擦力。这防止颗粒粘附于片剂冲压机(tablet punches),促进其从片剂冲压机中排出等。可使用的适当的润滑剂的实例包括但不限于滑石、硬脂酸、植物油、硬脂酸钙、硬脂酸锌、硬脂酸镁等。The lubricant reduces the friction between the particles and the mold wall during compression and discharge. This prevents the particles from adhering to the tablet punches, facilitating their discharge from the tablet press, and the like. Examples of suitable lubricants that may be used include, but are not limited to, talc, stearic acid, vegetable oils, calcium stearate, zinc stearate, magnesium stearate, and the like.
助流剂用于改善颗粒的流动特征。适当的助流剂的实例包括但不限于二氧化硅、玉米淀粉、微粉硅胶、滑石粉、聚乙二醇。Glidants are used to improve the flow characteristics of the particles. Examples of suitable glidants include, but are not limited to, silica, corn starch, micronized silica gel, talc, polyethylene glycol.
如果组合物的制备包括制粒步骤,则通常使用粘合剂,适当的粘合剂的实例包括但不限于吡咯烷酮、聚乙烯吡咯烷酮、黄原胶、纤维素胶如羧甲基纤维素、甲基纤维素、羟乙基纤维素、羟丙基纤维素、羟丙基甲基纤维素、羟基纤维素、明胶、淀粉和预胶化淀粉。If the preparation of the composition includes a granulation step, a binder is usually used, and examples of suitable binders include, but are not limited to, pyrrolidone, polyvinylpyrrolidone, xanthan gum, cellulose gum such as carboxymethylcellulose, methyl Cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropyl methylcellulose, hydroxy cellulose, gelatin, starch and pregelatinized starch.
崩解剂是指能使片剂在胃肠液中迅速裂碎成细小颗粒的物质,从而使功能成分迅速溶解吸收,发挥作用。本发明中所述崩解剂包括但不限于低取代羟丙基纤维素、交联羧 甲基纤维素钠、羧甲基淀粉钠以及交联聚维酮中的一种或者多种。The disintegrant refers to a substance which can rapidly break up a tablet into fine particles in a gastrointestinal fluid, so that the functional component dissolves and absorbs rapidly, and functions. The disintegrants described in the present invention include, but are not limited to, one or more of low-substituted hydroxypropylcellulose, croscarmellose sodium, sodium carboxymethyl starch, and crospovidone.
本发明提供的控释药物组合物,还可包含在该组合物中的其它赋形剂包括但不限于防腐剂、抗氧化剂或任何通常用于制药工业的其它赋形剂等。The controlled release pharmaceutical compositions provided herein, other excipients that may also be included in the compositions include, but are not limited to, preservatives, antioxidants, or any other excipients commonly used in the pharmaceutical industry, and the like.
本发明提供的组合物最终呈现为易于患者服用的药用形式,可选片剂或者胶囊。The compositions provided by the present invention are ultimately presented in a pharmaceutically acceptable form for administration to a patient, optionally as a tablet or capsule.
本发明所述的控释组合物推荐的给药方式为饭后服用。The recommended mode of administration of the controlled release compositions of the present invention is after meals.
本发明提供的控释药物组合物,其特征在于所述延迟释放漂浮组合物中活性药物在热熔挤出过程后任选保持晶型状态或者转变为无定型状态。The controlled release pharmaceutical composition of the present invention is characterized in that the active drug in the delayed release floating composition optionally remains in a crystalline state or is converted to an amorphous state after the hot melt extrusion process.
出于药效、安全性、经济性、便利性和/或效率,在本发明的药物组合物中使用单一药物可能是可取的,但应理解本发明组合物可包括不只一种的药物,即速释组分与延迟释放释漂浮组分中的药物相同或者不同。It may be desirable to use a single drug in the pharmaceutical compositions of the present invention for efficacy, safety, economy, convenience, and/or efficiency, but it should be understood that the compositions of the present invention may include more than one drug, ie, The immediate release component is the same as or different from the drug in the delayed release release component.
本发明还提供一种制备上述控释药物组合的方法。The present invention also provides a method of preparing the above controlled release drug combination.
本发明提供的制备控释药物组合物的方法包含以下步骤:1)在热熔挤出前将至少一种溶剂、延迟释放漂浮组分中活性成分和至少一种肠溶性聚合物混合得预混粗品或者热熔挤出过程中在线将至少一种溶剂、延迟释放漂浮组分中活性成分和至少一种肠溶性聚合物混合得预混粗品;2)预混粗品通过挤出机的加热螺杆区后经口模离开得挤出物。The method for preparing a controlled release pharmaceutical composition provided by the present invention comprises the steps of: 1) premixing at least one solvent, an active ingredient in a delayed release floating component, and at least one enteric polymer before hot melt extrusion. In the crude or hot melt extrusion process, at least one solvent, the active ingredient in the delayed release floating component and the at least one enteric polymer are mixed in advance to obtain a premixed crude product; 2) the premixed crude product passes through the heating screw zone of the extruder. After the die exits the extrudate.
本发明提供的制备方法,其特征在于所述溶剂只需要满足在热熔挤出过程结束后可以被挥发即可,优选的,本发明将溶剂的沸点限定为30-110℃。The preparation method provided by the present invention is characterized in that the solvent only needs to satisfy the fact that it can be volatilized after the end of the hot melt extrusion process. Preferably, the present invention limits the boiling point of the solvent to 30-110 °C.
本发明提供的制备方法,其特征在于所述溶剂选自水、甲醇、乙醇、异丙醇、丙酮、戊烷、己烷、庚烷、环己烷、二氯甲烷、四氢呋喃,优选水、乙醇、异丙醇。The preparation method provided by the present invention is characterized in that the solvent is selected from the group consisting of water, methanol, ethanol, isopropanol, acetone, pentane, hexane, heptane, cyclohexane, dichloromethane, tetrahydrofuran, preferably water, ethanol. , isopropanol.
本发明提供的方法中,所述溶剂的用量为0.1%-70%,优选1%-50%,最优选10%-30%(质量百分比,以固体组分的总质量为100计算)。In the process provided by the present invention, the solvent is used in an amount of from 0.1% to 70%, preferably from 1% to 50%, most preferably from 10% to 30% by mass based on the total mass of the solid component of 100.
本发明公开的方法中,口模前端加热区的温度应大于挤出混合物的玻璃化转变温度(Tg)。In the method disclosed herein, the temperature of the heated zone at the front end of the die should be greater than the glass transition temperature (Tg) of the extruded mixture.
本发明提供的制备方法,其特征在于口模温度为70-200℃,优选90-180℃,更优选110-160℃。The preparation method provided by the present invention is characterized in that the die temperature is from 70 to 200 ° C, preferably from 90 to 180 ° C, more preferably from 110 to 160 ° C.
本发明提供的制备方法,其特征在于溶剂注入螺杆区温度为10-90℃。The preparation method provided by the present invention is characterized in that the solvent injection screw zone temperature is 10-90 °C.
考虑到活性治疗剂本身的性质,本发明的部分方案中,若热熔挤出过程中选用水做溶剂时,则遇水易发生的降解的酯类(包括内酯)、酰胺类(包括内酰胺)及高温易分解的物质不作为本申请的活性药物。In view of the nature of the active therapeutic agent, in some parts of the present invention, if water is used as a solvent in the hot melt extrusion process, the esters (including lactones) and amides (including lactones) which are easily degraded by water are included. The amide) and the substance which is easily decomposed at a high temperature are not used as the active drug of the present application.
本发明提供的制备方法,其特征在于还包含任选以下的步骤:1)将挤出物冷却,2)将挤出物去溶剂;3)将挤出物切割。The preparation method provided by the present invention is characterized by further comprising the steps of: 1) cooling the extrudate, 2) removing the extrudate from the solvent; 3) cutting the extrudate.
本发明提供的方法中,根据溶剂本身的性质以及口模的温度,沸点低易挥发的溶剂在挤出过程中可基本上被挥发,沸点低易挥发的溶剂包括但不限于乙醇。In the method provided by the present invention, the solvent having a low boiling point and being relatively volatile may be substantially volatilized during extrusion according to the nature of the solvent itself and the temperature of the die, and the solvent having a low boiling point and being volatile is included, but not limited to, ethanol.
本发明中所述的基本上被挥发是指挤出物中溶剂残留量小于15%,优选小于12%,最优选小于10%。Substantially volatilized as used herein means that the residual amount of solvent in the extrudate is less than 15%, preferably less than 12%, and most preferably less than 10%.
本发明提供的方法,当选用沸点较高的溶剂时,可在热熔挤出结束后紧跟将挤出物去溶剂的步骤。The method provided by the present invention, when a solvent having a higher boiling point is selected, may be followed by a step of desolvating the extrudate after the end of hot melt extrusion.
在一些实施方案中,除去挤出物中溶剂在升温和/或真空条件下。In some embodiments, the solvent in the extrudate is removed under elevated temperature and/or vacuum conditions.
在一些实施方案中,升高的温度足以使溶剂由液态转化为气态即可。In some embodiments, the elevated temperature is sufficient to convert the solvent from a liquid to a gaseous state.
在一些实施方案中,除去挤出物中溶剂在减压条件下完成。In some embodiments, the solvent in the extrudate is removed under reduced pressure conditions.
在一些实施方案中,本发明提供的制备方法还包含将挤出物冷却的步骤。In some embodiments, the method of preparation provided by the present invention further comprises the step of cooling the extrudate.
本发明提供的制备控释药物组合物中控释漂浮组分的方法,其特征在于进一步包含挤出物被切割的步骤。The present invention provides a method of preparing a controlled release floating component in a controlled release pharmaceutical composition, characterized by further comprising the step of cutting the extrudate.
本发明所述的速释部分的制备方法包括湿法制粒、干法制粒、粉末直压等。The preparation method of the immediate release portion of the present invention includes wet granulation, dry granulation, powder direct pressing and the like.
本发明提供的制备方法,其特征在于所述挤出机选自单螺杆热熔挤出机、啮合螺杆挤出机、双螺杆热熔挤出机,优选双螺杆热熔挤出机。The preparation method provided by the present invention is characterized in that the extruder is selected from the group consisting of a single screw hot melt extruder, an intermeshing screw extruder, a twin screw hot melt extruder, preferably a twin screw hot melt extruder.
本发明中所用的术语“延迟释放”是指改进释放的类型,其中药物剂型在口服给药药物剂型和从所述剂型释放药物之间表现出时间延迟。通常,延延迟释放放剂型在预定时间内或者直到满足预定条件例如暴露于某种pH水平,几乎没有或没有释放活性化合物,然后在此后立即发生活性化合物的释放。The term "delayed release" as used in the present invention refers to a type of improved release wherein the pharmaceutical dosage form exhibits a time delay between oral administration of the pharmaceutical dosage form and release of the drug from the dosage form. Typically, the delayed release release dosage form will have little or no release of the active compound for a predetermined period of time or until predetermined conditions are met, such as exposure to a certain pH level, and then the release of the active compound occurs immediately thereafter.
本发明中术语“控释”是指延长释放制剂的类型,其中药物的逐渐释放在某个延长的时间段内是受控的或受操作的。The term "controlled release" in the context of the invention refers to a type of extended release formulation wherein the gradual release of the drug is controlled or manipulated for an extended period of time.
附图说明DRAWINGS
图1.制剂3、制剂4以及普通速释片的药时曲线图;Figure 1. Drug time profile of Formulation 3, Formulation 4, and conventional immediate release tablets;
图2.实施例1-7中得到的漂浮颗粒的溶出曲线图;Figure 2. Dissolution profile of the floating particles obtained in Examples 1-7;
图3.颗粒G的溶出曲线图;Figure 3. Dissolution profile of particle G;
图4.制剂3、制剂4以及普通速释片的溶出曲线图;Figure 4. Dissolution profiles of Formulation 3, Formulation 4, and conventional immediate release tablets;
图5.颗粒G的电镜扫描图;Figure 5. Electron microscopic scan of particle G;
图6.颗粒G中非布司他热熔挤出前后粉末衍射图。Figure 6. Powder diffraction pattern before and after non-clothes hot melt extrusion in granule G.
图7.实施例10挤出前后氢氯噻嗪的粉末衍射图谱;Figure 7. Powder diffraction pattern of hydrochlorothiazide before and after extrusion of Example 10;
图8.实施例10溶出曲线图;Figure 8. Example 10 dissolution profile;
图9.实施例11挤出前后氢氯噻嗪的粉末衍射图谱;Figure 9. Powder diffraction pattern of hydrochlorothiazide before and after extrusion in Example 11;
图10.实施例11溶出曲线图;Figure 10. Example 11 dissolution profile;
图11.实施例12挤出前后硝苯地平的粉末衍射图谱;Figure 11. Powder diffraction pattern of nifedipine before and after extrusion in Example 12;
图12.实施例12溶出曲线图;Figure 12. Example 12 dissolution profile;
图13.实施例13挤出前后他达拉非的粉末衍射图谱;Figure 13. Powder diffraction pattern of tadalafil before and after extrusion in Example 13;
图14.实施例13溶出曲线图;Figure 14. Example 13 dissolution profile;
图15.实施例14挤出前后氯沙坦的粉末衍射图谱;Figure 15. Powder diffraction pattern of losartan before and after extrusion of Example 14;
图16.实施例14溶出曲线图;Figure 16. Example 14 dissolution profile;
图17.实施例15溶出曲线图;Figure 17. Example 15 dissolution profile;
图18.实施例16溶出曲线图;Figure 18. Example 16 dissolution profile;
图19.实施例17溶出曲线图;Figure 19. Example 17 dissolution profile;
图20.实施例18溶出曲线图;Figure 20. Example 18 dissolution profile;
图21.实施例19挤出前后氢氯噻嗪的粉末衍射图谱;Figure 21. Powder diffraction pattern of hydrochlorothiazide before and after extrusion in Example 19;
图22.实施例19溶出曲线图;Figure 22. Example 19 dissolution profile;
图23.实施例20挤出前后氢氯噻嗪的粉末衍射图谱;Figure 23. Powder diffraction pattern of hydrochlorothiazide before and after extrusion of Example 20.
图24.实施例20溶出曲线图;Figure 24. Example 20 dissolution profile;
图25.实施例21挤出前后氯沙坦的粉末衍射图谱;Figure 25. Powder diffraction pattern of losartan before and after extrusion of Example 21;
图26.实施例21溶出曲线图;Figure 26. Example 21 dissolution profile;
图27.实施例22溶出曲线图。Figure 27. Example 22 dissolution profile.
具体实施方式detailed description
以下为本发明的具体实施方式,实施例是为进一步描述本发明而不是限制本发明,凡与本发明等效的技术方案均属于本发明的保护范围。The following is a specific embodiment of the present invention, and the embodiments are intended to further describe the present invention and not to limit the present invention, and all the technical solutions equivalent to the present invention belong to the protection scope of the present invention.
本发明实施例中所用HPMCAS购买自日本信越化学株式会社,热熔挤出仪为赛默飞的双螺杆热熔挤出仪器。The HPMCAS used in the examples of the present invention was purchased from Shin-Etsu Chemical Co., Ltd., and the hot melt extruder was Thermo Fisher's twin-screw hot melt extrusion instrument.
实施例1.由速释非布司他微片和在pH6以上释放药物的非布司他漂浮颗粒A组成的非布司他制剂1Example 1. Febuxostat 1 consisting of immediate release febuxostat microchips and febuxostat floating particles A which release the drug above pH 6
单个胶囊包含速释组分和延迟释放漂浮组分,速释组分为含8mg非布司他活性成分的微片,延迟释放漂浮组分为含32mg非布司他活性成分的颗粒A,颗粒A在pH6以上释放。速释非布司他微片由湿法制粒工艺制备,其处方组成列在下表1中。The single capsule comprises an immediate release component and a delayed release floating component, the immediate release component is a microtablet containing 8 mg of febuxostat active ingredient, and the delayed release floating component is a particulate A containing 32 mg of febuxostat active ingredient, granules A is released above pH 6. The immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is listed in Table 1 below.
表1.速释非布司他微片处方Table 1. Immediate release of febuxostat microchip prescription
  作用effect 8mg片8mg tablets
非布司他Febuxostat 主药Main drug 13.3%13.3%
乳糖lactose 填充剂Filler 35.0%35.0%
MCCMCC 填充剂Filler 27.3%27.3%
交联羧甲基纤维素纳Cross-linked carboxymethyl cellulose 崩解剂Disintegrator 10.8%10.8%
微粉硅胶Microsilica gel 助流剂Glidant 2.2%2.2%
HPMC-E5HPMC-E5 黏合剂Adhesive 3.6%3.6%
water 黏合剂溶剂Binder solvent  
羧甲基淀粉钠Carboxymethyl starch sodium 崩解剂Disintegrator 8.3%8.3%
硬脂酸镁Magnesium stearate 润滑剂Lubricant 1.2%1.2%
具体制备工艺:湿法制粒机制粒,将原辅料混合,加入粘合剂,搅拌,1500rpm切刀剪切后过筛,烘干至水分<3%,过30目筛,后采用创博C&C600B单冲压片机,4.76mm冲头压片。片重:理论61.5mg,实际控制在59-65mg,硬度约30N。The specific preparation process: wet granulation mechanism granules, mixing raw materials and auxiliary materials, adding binder, stirring, 1500 rpm cutting, sieving, drying, to moisture <3%, passing through 30 mesh sieve, and then using Chuangbo C&C600B single Stamping machine, 4.76mm punch press. Tablet weight: theory 61.5mg, the actual control is 59-65mg, the hardness is about 30N.
非布司他漂颗粒A由热熔挤出工艺制备,其处方组成列在下表2中。The febuxostat bleaching granule A was prepared by a hot melt extrusion process, the formulation of which is listed in Table 2 below.
表2.非布司他漂浮颗粒A处方Table 2. Formulation of febuxostat floating particles A
  含量(g)Content (g) 百分比percentage
非布司他Febuxostat 150150 25%25%
HPMCAS MGHPMCAS MG 450450 75%75%
称取非布司他和HPMCAS MG在混料机中混合均匀,热熔挤出仪(赛默飞),温度设置如表3。The febuxostat and HPMCAS MG were weighed and mixed uniformly in a blender, and the hot melt extruder (Simofly) was set as shown in Table 3.
表3.热熔挤出机温度(℃)Table 3. Hot melt extruder temperature (°C)
DieDie Zone8Zone8 Zone7Zone7 Zone6Zone6 Zone5Zone5 Zone4Zone4 Zone3Zone3 Zone2Zone2
140140 110110 9090 7070 4040 3030 3030 3030
具体在Zone4加乙醇,速度为700ul/min,Zone2喂料,速度为4g/min,螺杆的转速设定为100rpm,将挤出物切成段,后将挤出物60℃烘箱烘干2h,乙醇含量小于0.5%,烘干后粉碎至2mm。Specifically, adding ethanol to Zone 4, the speed is 700 ul/min, Zone 2 feeding, the speed is 4 g/min, the rotation speed of the screw is set to 100 rpm, the extrudate is cut into segments, and then the extrudate is oven-dried at 60 ° C for 2 h. The ethanol content is less than 0.5%, and is pulverized to 2 mm after drying.
实施例2.由速释非布司他微丸和在pH6以上快速释放药物的非布司他延迟释放漂浮颗粒B组成的非布司他制剂2Example 2. Febuxostat formulation consisting of immediate release febuxostat pellets and febuxostat delayed release floating particle B, which rapidly releases the drug above pH 6
单个胶囊包含速释组分和延迟释放漂浮组分,速释组分为含8mg非布司他活性成分 的微丸,胶囊的剩余部分包含共含32mg非布司他的非布司他延迟释放漂浮颗粒B,此延迟释放漂浮肠溶颗粒B在pH6以上快速释放。速释非布司他微丸由空白丸芯上药工艺制备,其处方组成如表4。A single capsule contains an immediate release component and a delayed release floating component, the immediate release component is a pellet containing 8 mg of febuxostat active ingredient, and the remainder of the capsule contains a delayed release of febuxostat containing 32 mg of febuxostat. Floating particles B, this delayed release of floating enteric particles B is rapidly released above pH 6. The immediate release febuxostat pellets were prepared by a blank pellet core drug preparation process, and the prescription composition is shown in Table 4.
表4.速释非布司他微丸处方组成:Table 4. Composition of immediate release febuxostat pellets:
  8mg微丸8mg pellets
非布司他Febuxostat 32%32%
糖丸Sugar pill 52%52%
羟丙甲纤维素Hypromellose 18%18%
非布司他控释漂浮颗粒B由热熔挤出工艺制备,其处方组成如表5。The febuxostat controlled release floating granules B were prepared by a hot melt extrusion process, and the formulation composition thereof is shown in Table 5.
表5.非布司他漂浮颗粒B处方Table 5. Formulation of febuxostat floating particles B
  含量 content
非布司他Febuxostat 25%25%
羟丙甲基纤维素Hydroxypropylmethylcellulose 60%60%
HPMCAS MGHPMCAS MG 15%15%
称取150g非布司他和90g HPMCAS MG以及360g羟丙甲基纤维素在混料机中混合均匀。热熔挤出机温度设置如表3,在热熔挤出机的Zone4加乙醇,速度为700ul/min,Zone2喂料,速度为4g/min,螺杆的转速设定为100rpm,将挤出物切成段,后将挤出物60℃烘箱烘干2h,乙醇含量<0.5%。烘干后粉碎至4mm,既得非布司他胃漂浮控释颗粒B。150 g of febuxostat and 90 g of HPMCAS MG and 360 g of hydroxypropylmethylcellulose were weighed and mixed uniformly in a blender. The temperature setting of the hot melt extruder was as shown in Table 3. The ethanol was added to the Zone 4 of the hot melt extruder at a speed of 700 ul/min, the Zone 2 was fed at a speed of 4 g/min, and the rotation speed of the screw was set to 100 rpm. After cutting into sections, the extrudate was oven-dried at 60 ° C for 2 h, and the ethanol content was <0.5%. After drying, it is pulverized to 4 mm, and the controlled release granule B of febuxostat is obtained.
实施例3.由20%速释非布司他微片和80%在pH5以上释放药物的非布司他漂浮颗粒C组成的非布司他制剂3Example 3. Febuxostat formulation consisting of 20% immediate release febuxostat microchip and 80% febuxostat floating particle C releasing drug above pH 5
单个胶囊包含速释组分和控释漂浮组分,速释组分为含8mg非布司他的微片,胶囊的剩余部分包含共含32mg非布司他胃漂浮颗粒C,此胃漂浮颗粒C在pH5以上释放。速释非布司他微片由湿法制粒工艺制备,其处方组成列在上表1中。非布司他控释漂浮颗粒C由热熔挤出工艺制备,其处方组成如表6。The single capsule comprises an immediate release component and a controlled release floating component, the immediate release component is a microtablet containing 8 mg of febuxostat, and the remainder of the capsule comprises a total of 32 mg of febuxostat gastric floating particles C, the gastric floating particles C is released above pH 5. The immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is listed in Table 1 above. The febuxostat controlled release floating granule C was prepared by a hot melt extrusion process, and its prescription composition is shown in Table 6.
表6.非布司他漂浮颗粒C处方Table 6. Formulation of febuxostat floating particles C
  含量 content
非布司他Febuxostat 25%25%
HPMCAS LGHPMCAS LG 75%75%
将150g非布司他和450g HPMCAS LG混合均匀后,进行热熔挤出,温度参数设置同制备颗粒A。热熔挤出机的Zone4加乙醇,速度为600ul/min,Zone2喂料,速度为2g/min,螺杆转速为60rpm,将挤出物切割成段,后将挤出物60℃烘箱烘干2h,乙醇含量<0.5%,烘干后粉碎至4mm长颗粒,既得非布司他漂浮颗粒C。After 150 g of febuxostat and 450 g of HPMCAS LG were uniformly mixed, hot melt extrusion was carried out, and the temperature parameter setting was the same as that of the preparation of the pellet A. The hot melt extruder's Zone4 was added with ethanol at a speed of 600 ul/min, Zone 2 was fed at a speed of 2 g/min, the screw speed was 60 rpm, the extrudate was cut into segments, and the extrudate was oven dried at 60 ° C for 2 h. The ethanol content is <0.5%, and after pulverization, it is pulverized to 4 mm long particles, and the febuxostat floating particles C are obtained.
实施例4由40%速释非布司他微片和60%在pH5以上释放药物的非布司他漂浮颗粒C组成的非布司他制剂4Example 4 is a febuxostat formulation consisting of 40% immediate release febuxostat microtablets and 60% febuxostat floating particles C which release the drug above pH 5
单个胶囊包含速释组分和控释漂浮组分,速释组分为含16mg非布司他的微片,胶囊的剩余部分包含共含24mg非布司他延迟释放漂浮颗粒C,此延迟释放漂浮控释颗粒C在pH5以上释放。速释非布司他微片由湿法制粒工艺制备,其处方组成列在上表1中,非布司他控释漂浮颗粒C同实施例3。The single capsule contains an immediate release component and a controlled release floating component, the immediate release component is a microchip containing 16 mg of febuxostat, and the remainder of the capsule contains a total of 24 mg of febuxostat delayed release floating particle C, which is delayed release. The floating controlled release granule C is released above pH 5. The immediate release febuxostat microchip was prepared by a wet granulation process, the formulation of which is listed in Table 1 above, and the febuxostat controlled release floating granule C was the same as in Example 3.
实施例5由速释非布司他微丸和延迟释放非布司他漂浮颗粒D组成的非布司他制剂5Example 5: a febuxostat formulation consisting of immediate release febuxostat pellets and delayed release febuxostat floating particles D 5
单个胶囊包含速释组分和控释漂浮组分,速释组分为含8mg非布司他活性成分的微丸,胶囊的剩余部分包含共含32mg非布司他的非布司他胃延迟释放漂浮颗粒D,此胃漂浮延迟释放颗粒D在胃液中漂浮的同时缓慢释放。速释非布司他微丸由空白丸芯上药工艺制备,其处方组成列在上表4中。A single capsule contains an immediate release component and a controlled release floating component. The immediate release component is a pellet containing 8 mg of febuxostat active ingredient, and the remainder of the capsule contains a delay of 32 mg of febuxostat containing 32 mg of febuxostat. The floating particles D are released, and the gastric floating delayed release particles D are slowly released while floating in the gastric juice. The immediate release febuxostat pellets were prepared by a blank pellet core drug preparation process, and the prescription compositions are listed in Table 4 above.
非布司他胃漂浮控释颗粒D由热熔挤出工艺制备,处方组成如表7。The febuxostat gastric floating controlled release granule D was prepared by a hot melt extrusion process, and the composition of the formulation is shown in Table 7.
表7.非布司他漂浮颗粒D处方Table 7. Formulation of febuxostat floating particles D
Figure PCTCN2018091103-appb-000006
Figure PCTCN2018091103-appb-000006
将非布司他与季胺基甲基丙烯酸酯共聚物B型及羟丙甲纤维素混合均匀后,在湿法制粒机中剪切,同时缓慢滴加柠檬酸三乙酯。将混合好的物料进行热熔挤出,温度参数设置同表3,在Zone4加乙醇,速度为1000ul/min,Zone2喂料,速度为4g/min,螺杆的转速设定为100rpm,将挤出物切成段,后将挤出物60℃烘箱烘干2h,乙醇含量<0.5%。烘干后粉碎至4mm长颗粒,既得非布司他胃漂浮控释颗粒D。After blending the febuxostat with the quaternary amino methacrylate copolymer type B and hypromellose, it was sheared in a wet granulator while slowly adding triethyl citrate dropwise. The mixed materials were hot melt extruded, the temperature parameters were set as in Table 3, ethanol was added in Zone 4, the speed was 1000 ul/min, Zone 2 was fed, the speed was 4 g/min, the screw speed was set to 100 rpm, and the extrusion was performed. The material was cut into sections, and then the extrudate was oven-dried at 60 ° C for 2 h, and the ethanol content was <0.5%. After drying, it is pulverized to 4 mm long granules, and the controlled release granule D of febuxostat is obtained.
实施例6由速释非布司他微片和在延迟释放非布司他漂浮颗粒E组成的非布司他制 剂6Example 6 is a non-busestat formulation consisting of an immediate release febuxostat microparticle and a delayed release of febuxostat floating particle E 6
单个胶囊包含速释组分和控释漂浮组分,速释组分为含8mg非布司他的微片,胶囊的剩余部分包含共含32mg非布司他延迟释放漂浮颗粒E,此胃漂浮控释颗粒E在胃液中漂浮的同时缓慢释放。速释非布司他微片由湿法制粒工艺制备,其处方组成列如表1。非布司他胃漂浮延迟释放颗粒E由热熔挤出工艺制备,其处方组成如表8。The single capsule contains an immediate release component and a controlled release floating component. The immediate release component is a microtablet containing 8 mg of febuxostat. The remainder of the capsule contains a total of 32 mg of febuxostat delayed release floating particles E, which floats on the stomach. The controlled release granule E is slowly released while floating in the gastric juice. The immediate release febuxostat microchips were prepared by a wet granulation process, and the formulation of the compositions is shown in Table 1. The febuxostat gastric floating delayed release granule E was prepared by a hot melt extrusion process, and its prescription composition is shown in Table 8.
表8.非布司他漂浮颗粒E处方Table 8. Formulation of febuxostat floating particles E
Figure PCTCN2018091103-appb-000007
Figure PCTCN2018091103-appb-000007
将非布司他与其他赋形剂按处方量混合均匀后进行热熔挤出,温度参数设置如表3。在Zone4加乙醇,速度为300ul/min,Zone2喂料,速度为4g/min,螺杆的转速设定为100rpm,将挤出物切成段,后将挤出物60℃烘箱烘干2h,乙醇含量<0.5%,粉碎至4mm长颗粒,既得非布司他胃漂浮控释颗粒E。The febuxostat was mixed with other excipients in a prescribed amount and then subjected to hot melt extrusion. The temperature parameters were set as shown in Table 3. Add ethanol to Zone4 at a rate of 300 ul/min, Zone2 feed at a speed of 4 g/min, set the screw speed to 100 rpm, cut the extrudate into sections, and then extrude the extrudate at 60 ° C for 2 h in ethanol. The content is <0.5%, pulverized to 4 mm long particles, and the obtained bupretaxer gastric floating controlled release granule E is obtained.
实施例7由速释非布司他微片和在控释非布司他漂浮颗粒F组成的非布司他制剂7Example 7 is a non-busestat formulation consisting of an immediate release febuxostat microparticle and a controlled release febuxostat floating particle F
单个胶囊包含速释组分和控释漂浮组分,速释组分为含8mg非布司他的微片,胶囊的剩余部分包含共含32mg非布司他胃漂浮颗粒F,此胃漂浮控释颗粒E在胃液中漂浮的同时缓慢释放。速释非布司他微片由湿法制粒工艺制备,其处方组成列在表1中。非布司他胃漂浮控释颗粒F由热熔挤出工艺制备,其处方组成如表9。The single capsule contains the immediate release component and the controlled release floating component, and the immediate release component is a microchip containing 8 mg of febuxostat. The remainder of the capsule contains a total of 32 mg of febuxostat floating particles F, which is controlled by the stomach. The release granule E is slowly released while floating in the gastric juice. The immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is listed in Table 1. The febuxostat gastric floating controlled release granule F was prepared by a hot melt extrusion process, and its formulation composition is shown in Table 9.
表9.非布司他漂浮颗粒F处方Table 9. Formulation of febuxostat floating particles F
Figure PCTCN2018091103-appb-000008
Figure PCTCN2018091103-appb-000008
将非布司他与其他赋形剂按处方量混合均匀后进行热熔挤出,温度参数设置如表3。在Zone4加乙醇,速度为300ul/min,Zone2喂料,速度为4g/min,螺杆的转速设定为 100rpm,将挤出物切成段,后将挤出物60℃烘箱烘干2h,乙醇含量<0.5%,烘干后粉碎至4mm长颗粒,既得非布司他胃漂浮控释颗粒F。The febuxostat was mixed with other excipients in a prescribed amount and then subjected to hot melt extrusion. The temperature parameters were set as shown in Table 3. Add ethanol to Zone4 at a rate of 300 ul/min, Zone2 feed at a speed of 4 g/min, set the screw speed to 100 rpm, cut the extrudate into sections, and then extrude the extrudate at 60 ° C for 2 h in ethanol. The content is <0.5%, and after pulverization, it is pulverized to 4 mm long particles, and the controlled release granule F of febuxostat is obtained.
实施例8由速释非布司他微片和在pH5.5以上释放药物的非布司他漂浮颗粒G组成的非布司他制剂8Example 8 is a febuxostat formulation consisting of an immediate release febuxostat microplatelet and a febuxostat floating particle G which releases the drug above pH 5.5.
单个胶囊包含速释组分和延迟释放漂浮组分,速释组分为含8mg非布司他活性成分的微片,延迟释放漂浮组分为含32mg非布司他活性成分的颗粒G,颗粒A在pH5.5以上释放。速释非布司他微片由湿法制粒工艺制备,其处方组成如表1,非布司他延迟释放漂浮颗粒G处方组成如表10,热熔挤出及温度设置如表11所示。The single capsule comprises an immediate release component and a delayed release floating component, the immediate release component is a microtablet containing 8 mg of febuxostat active ingredient, and the delayed release floating component is a particulate G containing 32 mg of febuxostat active ingredient, granules A is released above pH 5.5. The immediate release febuxostat microtablets were prepared by a wet granulation process, the formulation of which is shown in Table 1, and the formulation of febuxostat delayed release floating granules G is shown in Table 10. The hot melt extrusion and temperature settings are shown in Table 11.
表10.非布司他延迟释放漂浮颗粒GTable 10. Febuxostat delayed release floating particles G
  比例 proportion
非布司他Febuxostat 25%25%
HPMCAS LFHPMCAS LF 75%75%
Pharma11热熔挤出仪(赛默飞),设定温度如表11。Pharma11 hot melt extruder (Siomer), set the temperature as shown in Table 11.
表11.热熔挤出机温度设置(℃)Table 11. Hot melt extruder temperature setting (°C)
DieDie Zone8Zone8 Zone7Zone7 Zone6Zone6 Zone5Zone5 Zone4Zone4 Zone3Zone3 Zone2Zone2
140140 130130 100100 9090 8080 7070 6060 5050
具体在Zone2喂料,Zone4加水,喂料速度为5g/min,加水速度为0.9ml/min,螺杆转速设置为100rpm,挤出物切成段,后将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm,测试密度为0.5g/cm 3,将所得非布司他颗粒G与实施例1所得的非布司他微片灌胶囊,得非布司他制剂8。 Specifically, in Zone2 feeding, Zone4 is added with water, the feeding speed is 5g/min, the watering speed is 0.9ml/min, the screw rotation speed is set to 100rpm, the extrudate is cut into segments, and the extrudate is dried in an oven at 60°C for 2 hours. Moisture <3%, pulverized to 2 mm after drying, test density was 0.5 g/cm 3 , and the obtained febuxostat granule G and the febuxostat microderage obtained in Example 1 were filled into capsules to obtain febuxostat preparation. 8.
实施例9人体药代动力学研究Example 9 Human Pharmacokinetic Study
以市售40mg规格非布司他片作为参比制剂,与实施例3和实施例4所获得的制剂一同进行人体药代动力学研究,研究结果见下表12。The human pharmacokinetic study was carried out together with the preparations obtained in Example 3 and Example 4 using a commercially available 40 mg-sized febuxostat as a reference preparation, and the results of the study are shown in Table 12 below.
表12.不同制剂药代动力学参数Table 12. Pharmacokinetic parameters of different formulations
Figure PCTCN2018091103-appb-000009
Figure PCTCN2018091103-appb-000009
C max:最大血药峰浓度 C max : maximum peak plasma concentration
T max:最大血药浓度时间 T max : maximum blood concentration time
AUC 0→∞:药时曲线面积 AUC 0→∞ : drug time curve area
T C≥100μg/mL:有效血药浓度C≥100μg/mL时间 T C≥100μg/mL : effective blood concentration C≥100μg/mL time
Fr:相对生物利用度Fr: relative bioavailability
药代动力学研究结果表明,与市售非布司他片参比制剂相比,实施例3和实施例4能够降低药物的最大血药峰浓度,大幅延长作用时间,发挥药物的控释治疗作用,从而降低药物的副作用,结果如图1所示。The results of pharmacokinetic studies showed that Example 3 and Example 4 can reduce the maximum peak concentration of the drug compared with the commercially available febuxostat reference preparation, greatly prolong the duration of action, and exert controlled release of the drug. The effect, thereby reducing the side effects of the drug, the results are shown in Figure 1.
实验例1Experimental example 1
使用300mL的pH5.0FaSSGF为溶出介质,观察胃漂浮颗粒在模拟胃液下的漂浮情况,经观察,各颗粒均立即起漂,且长时间漂浮,观察至24小时后,各颗粒仍然维持漂浮,停止观察。300mL of pH5.0FaSSGF was used as the dissolution medium to observe the floating condition of the gastric floating particles under simulated gastric fluid. After observation, all the particles immediately floated and floated for a long time. After 24 hours, the particles remained floating and stopped. Observed.
根据中国药典2015版二部附录溶出检测方法1(篮法,100rpm,37℃),检测非布司他延迟释放漂浮颗粒A、颗粒B、颗粒C、颗粒D、颗粒E、颗粒F、颗粒G的溶出情况。Detection of febuxostat delayed release floating particle A, particle B, particle C, particle D, particle E, particle F, particle G according to the Chinese Pharmacopoeia 2015 edition two appendix dissolution test method 1 (basket method, 100 rpm, 37 ° C) Dissolution.
使用300mL的pH5.0FaSSGF为溶出介质,检测胃漂浮颗粒在模拟胃液下的溶出情况,再换用900mL的pH6.5FaSSIF为溶出介质,检测胃漂浮颗粒在模拟肠液下的溶出情况,结果如图2、图3(颗粒G)所示。300mL of pH5.0FaSSGF was used as the dissolution medium to detect the dissolution of gastric floating particles under simulated gastric juice, and then 900mL of pH6.5FaSSIF was used as the dissolution medium to detect the dissolution of gastric floating particles under simulated intestinal fluid. The results are shown in Fig. 2. Figure 3 (Particle G).
根据中国药典2015版二部附录溶出检测方法1(篮法,100rpm,37℃),使用900mL的pH 6.8的磷酸盐缓冲液为溶出介质,检测实施例3和实施例4中得到制剂3、制剂4及速释微片的溶出曲线,结果如图4所示。According to the Chinese Pharmacopoeia 2015 edition two appendix dissolution detection method 1 (basket method, 100 rpm, 37 ° C), 900 mL of phosphate buffer solution of pH 6.8 was used as the dissolution medium, and the preparations 3 and preparations obtained in Example 3 and Example 4 were tested. 4 and the dissolution profile of the immediate release microchip, the results are shown in Figure 4.
溶出速度可以提示制剂在胃肠道环境下药物从制剂出释放的速度,更低的释放速度反应在药动学数据上为更低的Cmax及更长的释放时间。与普通速释片相比,本发明中所制备的制剂溶出速率有明显降低,可推测出与速释片相比,本发明中的制剂(实施例1-7)均可实现降低Cmax值,延长有效血药浓度时间的目的。The rate of dissolution can indicate the rate at which the drug is released from the formulation in the gastrointestinal environment, and the lower rate of release response is a lower Cmax and longer release time on the pharmacokinetic data. Compared with the conventional immediate release tablets, the dissolution rate of the preparation prepared in the present invention is remarkably lowered, and it can be inferred that the preparations of the present invention (Examples 1 to 7) can achieve a lower Cmax value than the immediate release tablets. The purpose of extending the effective blood concentration time.
用电镜扫描观察颗粒G的性状,发现在电镜下颗粒G为多孔状,具体见图5。The traits of the particle G were observed by scanning electron microscopy, and it was found that the particle G was porous under the electron microscope, as shown in Fig. 5.
对于非布司他原料及挤出后非布司他的晶型状态测试粉末衍射图谱,具体如图6所示,热熔挤出后非布司他依旧保持为晶型状态。The powder diffraction pattern for the crystalline state of the febuxostat and the non-busestat after extrusion, as shown in Fig. 6, is maintained in a crystalline state after hot melt extrusion.
实施例10氢氯噻嗪(30mg处方)氢氯噻嗪:HPMC AS LG=1:3Example 10 Hydrochlorothiazide (30 mg prescription) Hydrochlorothiazide: HPMC AS LG = 1:3
将氢氯噻嗪和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表13(℃)。The hydrochlorothiazide and HPMC AS LG were uniformly mixed and subjected to hot melt extrusion, and the temperature parameters were set as shown in Table 13 (° C.).
表13.Table 13.
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7Zone7 Zone8Zone8 DieDie
3030 5050 6060 7070 9090 9090 100100 120120
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为400ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 400 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:挤出顺利,工艺稳定,样品膨胀,能迅速起漂。Phenomenon: The extrusion is smooth, the process is stable, the sample is expanded, and it can be quickly floated.
对于氢氯噻嗪原料及实施例10中挤出后氢氯噻嗪的晶型状态测试粉末衍射图谱,热熔挤出后氢氯噻嗪依旧保持为晶型状态,如图7所示;实施例10处方的溶出曲线如图8所示。The powder diffraction pattern of the hydrochlorothiazide starting material and the crystalline state of the hydrochlorothiazide after extrusion in Example 10, the hydrochlorothiazide remained in a crystalline state after hot melt extrusion, as shown in FIG. 7; the dissolution profile of the formulation of Example 10 is shown in FIG. Shown.
实施例11氢氯噻嗪(30mg处方)氢氯噻嗪:HPMCP=1:3Example 11 Hydrochlorothiazide (30 mg prescription) Hydrochlorothiazide: HPMCP = 1:3
将氢氯噻嗪和HPMCP混合均匀,进行热熔挤出,温度参数设置如表14(℃)。Hydrochlorothiazide and HPMCP were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 14 (°C).
表14.Table 14.
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
4040 5050 6060 7070 8080 8080 100100 130130
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为500ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 500 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:样品挤出顺利,且能迅速起漂。Phenomenon: The sample is extruded smoothly and can be quickly floated.
对于氢氯噻嗪原料及实施例11中挤出后氢氯噻嗪的晶型状态测试粉末衍射图谱,热熔挤出后氢氯噻嗪依旧保持为晶型状态,如图9所示;实施例11处方的溶出曲线如图10所示。For the hydrochlorothiazide starting material and the crystal form test powder diffraction pattern of the hydrochlorothiazide after extrusion in Example 11, hydrochlorothiazide remained in a crystalline state after hot melt extrusion, as shown in FIG. 9; the dissolution profile of the formulation of Example 11 is shown in FIG. Shown.
实施例12硝苯地平(30mg处方)硝苯地平:HPMC AS LG=1:3Example 12 Nifedipine (30 mg prescription) Nifedipine: HPMC AS LG = 1:3
将硝苯地平和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表15(℃)。Nifedipine and HPMC AS LG were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 15 (°C).
表15.Table 15.
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
4040 5050 6060 8080 8080 8080 110110 130130
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为1200ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 1200 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:样品挤出顺利,且能迅速起漂。Phenomenon: The sample is extruded smoothly and can be quickly floated.
对于硝苯地平原料及实施例12中挤出后硝苯地平的晶型状态测试粉末衍射图谱,热熔挤出后硝苯地平依旧保持为晶型状态,如图11所示;实施例12处方的溶出曲线如图12所示。The powder diffraction pattern of the nifedipine starting material and the crystalline state of the nifedipine after extrusion in Example 12, the nifedipine remained in a crystalline state after hot melt extrusion, as shown in FIG. 11; The dissolution profile is shown in Figure 12.
实施例13他达拉非(30mg处方)他达拉非:HPMC AS LG=1:3Example 13 Tadalafil (30 mg prescription) Tadalafil: HPMC AS LG = 1:3
将他达拉非和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表16(℃)。The tadalafil and HPMC AS LG were mixed uniformly for hot melt extrusion, and the temperature parameters were set as shown in Table 16 (°C).
表16.Table 16.
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 4040 4040 5050 7070 9090 110110 130130
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为900ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 900 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:挤出顺利,工艺稳定,样品膨胀,能迅速起漂。Phenomenon: The extrusion is smooth, the process is stable, the sample is expanded, and it can be quickly floated.
对于他达拉非原料及实施例13中挤出后他达拉非的晶型状态测试粉末衍射图谱,热熔挤出后他达拉非依旧保持为晶型状态,如图13所示;实施例13处方的溶出曲线如图14所示。The powder diffraction pattern of the tadalafil raw material and the crystalline state of the tadalafil after extrusion in Example 13 was maintained, and the tadalafil remained in a crystalline state after hot melt extrusion, as shown in FIG. 13; The dissolution profile of the formulation of Example 13 is shown in FIG.
实施例14氯沙坦(30mg处方)氯沙坦:HPMC AS LG=1:3Example 14 Losartan (30 mg prescription) Losartan: HPMC AS LG = 1:3
将氯沙坦和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表17(℃)。The losartan and HPMC AS LG were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 17 (°C).
表17Table 17
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 5050 6060 8080 8080 9090 100100 130130
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为600ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 600 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:挤出顺利,样品膨胀,能迅速起漂。Phenomenon: The extrusion is smooth, the sample is expanded, and it can be quickly floated.
对于氯沙坦原料及实施例14中挤出后氯沙坦的晶型状态测试粉末衍射图谱,热熔挤出后氯沙坦依旧保持为晶型状态,如图15所示;实施例14处方的溶出曲线如图16所示。The powder diffraction pattern of the losartan raw material and the crystalline state of losartan after extrusion in Example 14 was maintained, and the losartan remained in a crystalline state after hot melt extrusion, as shown in FIG. 15; The dissolution profile is shown in Figure 16.
实施例15(地塞米松30mg处方)地塞米松:HPMC AS LG=1:3Example 15 (dexamethasone 30 mg prescription) dexamethasone: HPMC AS LG = 1:3
将地塞米松和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表18(℃)。The dexamethasone and HPMC AS LG were mixed uniformly and hot melt extruded. The temperature parameters were set as shown in Table 18 (°C).
表18Table 18
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 5050 6060 8080 8080 9090 100100 130130
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为400ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 400 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:挤出顺利,样品膨胀,能迅速起漂。Phenomenon: The extrusion is smooth, the sample is expanded, and it can be quickly floated.
实施例15处方的溶出曲线如图17所示。The dissolution profile of the formulation of Example 15 is shown in FIG.
实施例16地塞米松(30mg处方)地塞米松:HPMCP=1:3Example 16 Dexamethasone (30 mg Prescription) Dexamethasone: HPMCP = 1:3
将地塞米松和HPMCP混合均匀,进行热熔挤出,温度参数设置如表19(℃)。The dexamethasone and HPMCP were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 19 (°C).
表19Table 19
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
4040 5050 6060 7070 8080 8080 100100 140140
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为400ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water addition speed is 400 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:挤出顺利,样品表面膨胀,气泡在表面破裂,但是能迅速起漂。Phenomenon: The extrusion is smooth, the surface of the sample expands, and the bubbles rupture on the surface, but can quickly float.
实施例16处方的溶出曲线如图18所示。The dissolution profile of the formulation of Example 16 is shown in FIG.
实施例17呋塞米(30mg处方)呋塞米:HPMC AS LG=1:3Example 17 Furosemide (30 mg prescription) furosemide: HPMC AS LG = 1:3
将呋塞米和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表20(℃)。Furosemide and HPMC AS LG were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 20 (°C).
表20Table 20
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 5050 6060 8080 8080 9090 100100 130130
具体在Zone2喂料,Zone4加水,螺杆转速设置为50rpm,加水速度为600ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 50 rpm, the water adding speed is 600 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:挤出顺利,样品膨胀,能迅速起漂。Phenomenon: The extrusion is smooth, the sample is expanded, and it can be quickly floated.
实施例17处方的溶出曲线如图19所示。The dissolution profile of the formulation of Example 17 is shown in FIG.
实施例18非布司他(30mg)非布司他:HPMCP=1:3Example 18 febuxostat (30 mg) febuxostat: HPMCP = 1:3
将非布司他和HPMCP混合均匀,进行热熔挤出,温度参数设置如表21(℃)。The febuxostat and HPMCP were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 21 (°C).
表21Table 21
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
4040 5050 6060 7070 8080 8080 100100 130130
具体在Zone2喂料,Zone4加水,螺杆转速设置为100rpm,加水速度为700-900ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 is added with water, the screw rotation speed is set to 100 rpm, the water adding speed is 700-900 ul/min, the extrudate is oven-dried at 60 ° C for 2 h, the water content is <3%, and the pulverization is 2 mm after drying.
现象:样品能够膨胀,且样品能够漂浮。Phenomenon: The sample can expand and the sample can float.
实施例18处方的溶出曲线如图20所示。The dissolution profile of the formulation of Example 18 is shown in FIG.
实施例19氢氯噻嗪(30mg处方)氢氯噻嗪:HPMC AS LG=1:3Example 19 Hydrochlorothiazide (30 mg prescription) Hydrochlorothiazide: HPMC AS LG = 1:3
将氢氯噻嗪和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表22(℃)。Hydrochlorothiazide and HPMC AS LG were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 22 (°C).
表22Table 22
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 3030 4040 5050 8080 9090 110110 130130
具体在Zone2喂料,Zone4加乙醇,螺杆转速设置为60rpm,加乙醇速度为700ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 plus ethanol, the screw rotation speed was set to 60 rpm, the ethanol speed was 700 ul/min, the extrudate was oven-dried at 60 ° C for 2 h, the moisture was <3%, and the pulverization was 2 mm after drying.
现象:挤出顺利,工艺稳定,样品膨胀,能迅速起漂。Phenomenon: The extrusion is smooth, the process is stable, the sample is expanded, and it can be quickly floated.
对于氢氯噻嗪原料及实施例19中挤出后氢氯噻嗪的晶型状态测试粉末衍射图谱,热熔挤出后氢氯噻嗪依旧保持为晶型状态,如图21所示;实施例19处方的溶出曲线如图22所示。For the hydrochlorothiazide starting material and the crystal form test powder diffraction pattern of the hydrochlorothiazide after extrusion in Example 19, hydrochlorothiazide remained in a crystalline state after hot melt extrusion, as shown in FIG. 21; the dissolution profile of the formulation of Example 19 is shown in FIG. Shown.
实施例20氢氯噻嗪(30mg处方)氢氯噻嗪:HPMCP=1:3Example 20 Hydrochlorothiazide (30 mg prescription) Hydrochlorothiazide: HPMCP = 1:3
将氢氯噻嗪和HPMCP混合均匀,进行热熔挤出,温度参数设置如表23(℃)。The hydrochlorothiazide and HPMCP were uniformly mixed and subjected to hot melt extrusion, and the temperature parameters were set as shown in Table 23 (° C.).
表23Table 23
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 3030 4040 5050 8080 9090 110110 130130
具体在Zone2喂料,Zone4加乙醇,螺杆转速设置为50rpm,加乙醇速度为700ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 plus ethanol, the screw rotation speed was set to 50 rpm, the ethanol speed was 700 ul/min, the extrudate was oven-dried at 60 ° C for 2 h, the moisture was <3%, and the pulverization was 2 mm after drying.
现象:样品挤出顺利,且能迅速起漂。Phenomenon: The sample is extruded smoothly and can be quickly floated.
对于氢氯噻嗪原料及实施例20挤出后氢氯噻嗪的晶型状态测试粉末衍射图谱,热熔挤出后氢氯噻嗪依旧保持为晶型状态,如图23所示;实施例20处方的溶出曲线如图24所示。The powder diffraction pattern of the hydrochlorothiazide starting material and the crystal form state of hydrochlorothiazide after extrusion in Example 20, the hydrochlorothiazide remained in a crystalline state after hot melt extrusion, as shown in FIG. 23; the dissolution profile of the formulation of Example 20 is shown in FIG. Show.
实施例21氯沙坦(30mg处方)氯沙坦:HPMC AS LG=1:3Example 21 Losartan (30 mg prescription) Losartan: HPMC AS LG = 1:3
将氯沙坦和HPMC AS LG混合均匀,进行热熔挤出,温度参数设置如表24(℃)。The losartan and HPMC AS LG were mixed uniformly for hot melt extrusion, and the temperature parameters were set as shown in Table 24 (°C).
表24Table 24
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 3030 4040 5050 8080 9090 110110 130130
具体在Zone2喂料,Zone4加乙醇,螺杆转速设置为50rpm,加乙醇速度为700ul/min,将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, in Zone2 feeding, Zone4 plus ethanol, the screw rotation speed was set to 50 rpm, the ethanol speed was 700 ul/min, the extrudate was oven-dried at 60 ° C for 2 h, the moisture was <3%, and the pulverization was 2 mm after drying.
现象:样品挤出顺利,且能迅速起漂。Phenomenon: The sample is extruded smoothly and can be quickly floated.
对于氯沙坦原料及实施例21挤出后氯沙坦的晶型状态测试粉末衍射图谱,热熔挤出后氯沙坦依旧保持为晶型状态,如图25所示;实施例21处方的溶出曲线如图26所示。The powder diffraction pattern of the losartan raw material and the crystal form state of losartan after extrusion in Example 21 was maintained, and the losartan remained in a crystalline state after hot melt extrusion, as shown in FIG. 25; The dissolution profile is shown in Figure 26.
实施例22非布司他(30mg处方)非布司他:HPMCP=1:3Example 22 febuxostat (30 mg prescription) febuxostat: HPMCP = 1:3
将非布司他和HPMCP混合均匀,进行热熔挤出,温度参数设置如表25(℃)。The febuxostat and HPMCP were uniformly mixed and hot melt extruded. The temperature parameters were set as shown in Table 25 (°C).
表25Table 25
Zone2Zone2 Zone3Zone3 Zone4Zone4 Zone5Zone5 Zone6Zone6 Zone7 Zone7 Zone8Zone8 DieDie
3030 3030 4040 5050 8080 9090 110110 130130
具体在Zone2喂料,Zone4加乙醇,螺杆转速设置为50rpm,加乙醇速度为700/min, 将挤出物60℃烘箱烘干2h,水分<3%,烘干后粉碎至2mm。Specifically, the Zone2 feed, Zone4 plus ethanol, the screw rotation speed was set to 50 rpm, the ethanol speed was 700/min, the extrudate was oven-dried at 60 ° C for 2 h, the moisture was <3%, and the pulverization was 2 mm after drying.
现象:样品能够膨胀且样品能够漂浮。Phenomenon: The sample can expand and the sample can float.
实施例22处方的溶出曲线如图27所示。The dissolution profile of the formulation of Example 22 is shown in FIG.
虽然以上描述了本发明的具体实施方式,但是本领域的技术人员应当理解,这些仅是举例说明,在不背离本发明的原理和实质的前提下,可以对这些实施方式做出多种变更或修改。因此,本发明的保护范围由所附权利要求书限定。While the invention has been described with respect to the preferred embodiments of the embodiments of the embodiments of the invention modify. Accordingly, the scope of the invention is defined by the appended claims.

Claims (33)

  1. 一种控释药物组合物,包含:a)含有活性药物的速释组分,b)含有活性药物的延迟释放漂浮组分,其特征在于所述延迟释放漂浮组分通过热熔挤出的方法制备。A controlled release pharmaceutical composition comprising: a) an immediate release component comprising an active drug, b) a delayed release floating component comprising an active drug, characterized in that the delayed release floating component is extruded by hot melt preparation.
  2. 根据权利要求1所述的控释药物组合物,其特征在于所述的延迟释放漂浮组分含有至少一种肠溶性聚合物。The controlled release pharmaceutical composition according to claim 1, wherein said delayed release floating component contains at least one enteric polymer.
  3. 根据权利要求2所述的控释药物组合物,其特征在于所述的肠溶性聚合物选自聚乙烯醇乙酸苯二甲酸酯、邻苯二甲酸乙酸纤维素、1,2,4-苯三甲酸乙酸纤维素、邻苯二甲酸羟丙基甲基纤维素、1,2,4-苯三甲酸羟丙基甲基纤维素、琥珀酸乙酸纤维素、醋酸羟丙甲纤维素琥珀酸酯、醋酸羟丙基甲基纤维素酞酸酯、甲基丙烯酸-丙烯酸乙酯共聚物、甲基乙烯基醚-马来酸酐共聚物、甲基丙烯酸-丙烯酸乙酯共聚物水分散体、甲基丙烯酸-甲基丙烯酸甲酯共聚物、丙烯酸乙酯-甲基丙烯酸甲酯-甲基丙烯酸氯化三甲胺基乙酯共聚物、聚乙酸乙烯酯、乙基纤维素、聚醋酸乙烯酯与聚乙烯吡咯烷酮K30混合物,优选醋酸羟丙甲纤维素琥珀酸酯、甲基丙烯酸-甲基丙烯酸甲酯共聚物、甲基丙烯酸-丙烯酸乙酯共聚物、邻苯二甲酸羟丙基甲基纤维素。The controlled release pharmaceutical composition according to claim 2, wherein said enteric polymer is selected from the group consisting of polyvinyl alcohol acetate phthalate, cellulose acetate phthalate, 1,2,4-benzene Cellulose triacetate, hydroxypropyl methylcellulose phthalate, hydroxypropyl methylcellulose 1,2,4-benzenetricarboxylate, cellulose acetate succinate, hypromellose acetate succinate , hydroxypropyl methylcellulose phthalate acetate, methacrylic acid-ethyl acrylate copolymer, methyl vinyl ether-maleic anhydride copolymer, methacrylic acid-ethyl acrylate copolymer aqueous dispersion, methyl Acrylic-methyl methacrylate copolymer, ethyl acrylate-methyl methacrylate-trimethylaminoethyl methacrylate copolymer, polyvinyl acetate, ethyl cellulose, polyvinyl acetate and polyethylene A mixture of pyrrolidone K30, preferably hypromellose acetate succinate, methacrylic acid-methyl methacrylate copolymer, methacrylic acid-ethyl acrylate copolymer, hydroxypropyl methylcellulose phthalate.
  4. 根据权利要求2或3所述的控释药物组合物,其特征在于所述延迟释放漂浮组分中活性药物与肠溶性聚合物比例选自1:0.1-1:100,优选1:0.1-1:50,更优选1:1-1:25。The controlled release pharmaceutical composition according to claim 2 or 3, wherein the ratio of the active drug to the enteric polymer in the delayed release floating component is selected from 1:0.1 to 1:100, preferably 1:0.1-1 : 50, more preferably 1:1 to 1:25.
  5. 根据权利要求1-4任一项所述的控释药物组合物,其特征在于在所述热熔挤出前或者热熔挤出过程中加入溶剂。The controlled release pharmaceutical composition according to any one of claims 1 to 4, characterized in that a solvent is added before the hot melt extrusion or during the hot melt extrusion.
  6. 根据权利要求5所述的控释药物组合物,其特征在于所述溶剂沸点选自30-110℃。The controlled release pharmaceutical composition according to claim 5, wherein the solvent has a boiling point selected from the group consisting of 30 to 110 °C.
  7. 根据权利要求6所述的控释药物组合物,其特征在于所述溶剂选自水、甲醇、乙醇、异丙醇、丙酮、戊烷、己烷、庚烷、环己烷、二氯甲烷、四氢呋喃的至少一种,优选水、乙醇。The controlled release pharmaceutical composition according to claim 6, wherein the solvent is selected from the group consisting of water, methanol, ethanol, isopropanol, acetone, pentane, hexane, heptane, cyclohexane, dichloromethane, At least one of tetrahydrofuran is preferably water or ethanol.
  8. 根据权利要求1-7任一项所述的控释药物组合物,其特征在于所述延迟释放漂浮组分含有遇酸产生气体的碱性物质,所述碱性物质选自碳酸氢钠、碳酸钠、氨基乙酸钠碳酸盐、碳酸氢钾、碳酸镁和碳酸钙,优选碳酸钠、碳酸氢钠。The controlled release pharmaceutical composition according to any one of claims 1 to 7, wherein the delayed release floating component contains an alkaline substance which is in contact with an acid generating gas, and the basic substance is selected from the group consisting of sodium hydrogencarbonate and carbonic acid. Sodium, sodium aminoacetate carbonate, potassium hydrogencarbonate, magnesium carbonate and calcium carbonate are preferably sodium carbonate or sodium hydrogencarbonate.
  9. 根据权利要求1-8任一项所述的控释药物组合物,其特征在于所述延迟释放漂浮组分为多单元形式。The controlled release pharmaceutical composition according to any one of claims 1 to 8, characterized in that the delayed release floating component is in a multi-unit form.
  10. 根据权利要求9所述的控释药物组合物,其特征在于所述多单元形式为微片、微丸、颗粒,优选颗粒。The controlled release pharmaceutical composition according to claim 9, wherein the multi unit form is a microtablet, a pellet, a granule, preferably a granule.
  11. 根据权利要求1-7任一项所述的控释药物组合物,其特征在于所述延迟释放漂浮 组分为多孔状。The controlled release pharmaceutical composition according to any one of claims 1 to 7, wherein the delayed release floating component is porous.
  12. 根据权利要求1-7任一项所述的控释药物组合物,其特征在于所述延迟释放漂浮组分在pH5.0的FaSSGF溶液中立即起漂。The controlled release pharmaceutical composition according to any one of claims 1 to 7, wherein the delayed release floating component is immediately floated in a FaSSGF solution at pH 5.0.
  13. 根据权利要求1-7任一项所述的控释组合物,其特征在于所述延迟释放漂浮组分在pH5.0的FaSSGF溶液中漂浮时间大于24h。The controlled release composition according to any one of claims 1 to 7, wherein the delayed release floating component floats in a FaSSGF solution at pH 5.0 for more than 24 hours.
  14. 根据权利要求1-7任一项所述控释药物组合物,其特征在于所述延迟释放漂浮组分密度为0.1-1.0g/cm 3,优选0.2-0.8g/cm 3,最优选0.3-0.7g/cm 3The controlled release pharmaceutical composition according to any one of claims 1 to 7, characterized in that the delayed release floating component has a density of from 0.1 to 1.0 g/cm 3 , preferably from 0.2 to 0.8 g/cm 3 , most preferably 0.3- 0.7 g/cm 3 .
  15. 根据权利要求1-8任一项所述控释药物组合物,其特征在于所述延迟释放漂浮组分在300mL的pH5.0的FaSSGF溶出介质中,篮法,37℃,100rpm,5h的累积溶出小于30%,更优选小于20%,最优选小于10%。The controlled release pharmaceutical composition according to any one of claims 1-8, characterized in that the delayed release floating component is accumulated in 300 mL of FaSSGF dissolution medium at pH 5.0, basket method, 37 ° C, 100 rpm, 5 h The dissolution is less than 30%, more preferably less than 20%, and most preferably less than 10%.
  16. 根据权利要求1-8任一项所述的控释药物组合物,其特征在于所述延迟释放漂浮组分中活性药物选自BCSⅠ类药物。The controlled release pharmaceutical composition according to any one of claims 1 to 8, characterized in that the active drug in the delayed release floating component is selected from the group consisting of BCSI drugs.
  17. 根据权利要求16所述的控释药物组合物,其特征在于所述BCSⅠ类药物选自帕比司他、Cobimetinib、Patiromer、omarigliptin、安非他酮、胍法辛、文拉法辛盐酸盐、盐酸哌甲酯、磷酸泰地唑胺、氟班色林、eliglustat、阿格列汀、富马酸二甲酯、吡仑帕奈、洛美他派、卢索替尼、氯巴占、dalfampridine、Prolia、决奈达隆盐酸盐、Pralatrexate、lacosamide、fesoterodine fumarate、阿普唑仑、阿米替林盐酸盐、氨氯地平苯磺酸盐、贝那普利、阿莫西林、阿那曲唑、氮卓斯汀、比索洛尔、丁螺环酮、咖啡因、卡比多巴、西替利嗪、磷酸氯喹、扑尔敏、克林霉素、可乐定、环苯扎林、环磷酰胺、去氧孕烯、炔雌醇、地西泮、苯海拉明、多奈哌齐盐酸盐、多沙唑嗪甲磺酸盐、多西环素、恩曲他滨、雌二醇、乙琥胺、非索非那定、非那雄胺、氟康唑、氟胞嘧啶、氟西汀盐酸盐、氟伏沙明甲磺酸盐、丙咪嗪、吲达帕胺、异烟肼、拉米夫定、利多卡因、劳拉西泮、氯沙坦、琥珀酸美托洛尔、美西律、咪达唑仑、米氮平、孟鲁司特钠、炔诺酮、甲基炔诺酮、去甲替林、奥洛他定盐酸盐、奥司他韦、普拉克索、普伐他汀钠、强的松、泼尼松龙、普瑞巴林、普鲁卡因胺盐酸盐、异丙嗪盐酸盐、普萘洛尔盐酸盐、吡嗪酰胺、吡哆醇盐酸盐、喹那普利盐酸盐、奎尼丁、奎宁盐酸盐、雷米普利、舍曲林、枸橼酸西地那非、索他洛尔、司他夫定、特比萘芬盐酸盐、托特罗定、托拉塞米、曲马朵盐酸盐、曲唑酮、伐尼克兰、齐多夫定、阿法骨化醇、贝前列素、比哌立登、溴苯那敏、溴替唑仑、卡比沙明、克罗米芬、氯米帕明、氯唑西林、地尔硫卓、多拉司琼、吗丁啉、盐酸乙哌立松、依匹斯汀、钙化醇、麦角新碱、麦角胺、乙炔雌二醇、依替唑仑、氟伐他汀、格拉司琼、酮替芬、左旋咪唑、左炔诺孕酮、立马前列素、洛索洛芬、甲氟喹、盐酸美西律、尼卡 地平、氯硝柳胺、妥布特罗、甲氧苄啶、曲美布汀、托瑞米芬、特比萘芬、替莫普利、坦索罗辛、舍曲林、盐酸沙格雷酯、沙奎那韦、罗格列酮、利血平、雷米普利、盐酸丙哌维林、异丙嗪、培高利特、帕罗西汀。The controlled release pharmaceutical composition according to claim 16, wherein the BCSI-based drug is selected from the group consisting of pabisstat, Cobimetinib, Patiromer, omarigliptin, bupropion, guanfacine, venlafaxine hydrochloride , methylphenidate hydrochloride, tertimazine phosphate, flurbanin, eliglustat, alogliptin, dimethyl fumarate, pyrenoprene, lometan, rosotinib, clozab, Dalfampridine, Prolia, dronedarone hydrochloride, Pralattrexate, lacosamide, fesoterodine fumarate, alprazolam, amitriptyline hydrochloride, amlodipine besylate, benazepril, amoxicillin, ar Natrozole, azelastine, bisoprolol, buspirone, caffeine, carbidopa, cetirizine, chloroquine phosphate, chlorpheniramine, clindamycin, clonidine, cyclobenzaprine, Cyclophosphamide, desogestrel, ethinyl estradiol, diazepam, diphenhydramine, donepezil hydrochloride, doxazosin mesylate, doxycycline, emtricitabine, estradiol, Ethyl succinate, fexofenadine, finasteride, fluconazole, flucytosine, fluoxetine hydrochloride, fluvoxamine Sulfonate, imipramine, indapamide, isoniazid, lamivudine, lidocaine, lorazepam, losartan, metoprolol succinate, mexiletine, midazolam , mirtazapine, montelukast sodium, norethisterone, norgestrel, nortriptyline, olopatadine hydrochloride, oseltamivir, pramipexole, pravastatin sodium, strong Pine, prednisolone, pregabalin, procainamide hydrochloride, promethazine hydrochloride, propranolol hydrochloride, pyrazinamide, pyridoxine hydrochloride, quinapril Hydrochloride, quinidine, quinine hydrochloride, ramipril, sertraline, sildenafil citrate, sotalol, stavudine, terbinafine hydrochloride, care Trojan, torasemide, tramadol hydrochloride, trazodone, varenicline, zidovudine, alfacalcidol, beraprost, biperiden, brompheniramine, bromine Tazolam, carbyzamine, clomiphene, clomipramine, cloxacillin, diltiazem, dolasetron, morphine, eperisone hydrochloride, eplestine, calciferol, ergometrine, ergotamine , ethinyl estradiol, etidazolam, fluoride Rutastatin, granisetron, ketotifen, levamisole, levonorgestrel, ermaspirin, loxoprofen, mefloquine, mexiletine hydrochloride, nicardipine, niclosamide, tobex Luo, trimethoprim, trimebutine, toremifene, terbinafine, temocapril, tamsulosin, sertraline, sarpogrelate hydrochloride, saquinavir, rosiglitazone , reserpine, ramipril, propiverine hydrochloride, promethazine, pergolide, paroxetine.
  18. 根据权利要求1-8所述的控释药物组合物,其特征在于所述延迟释放漂浮组分中活性药物选自BCSⅡ至Ⅳ类药物。The controlled release pharmaceutical composition according to any one of claims 1 to 8, characterized in that the active drug in the delayed release floating component is selected from the group consisting of BCSII to IV drugs.
  19. 根据权利要求18所述的控释药物组合物,其特征在于所述BCSⅡ至Ⅳ类药物选自非布司他、ixazomib、Alectinib、Erismodegib、凡德他尼、阿瑞匹坦、硫酸沃拉帕沙、阿司匹林、二甲双胍、恩格列净、利格列汀、纳曲酮、dasabuvir、索非布韦、安非他明、依曲韦林、依维莫司、伊曲康唑、维罗非尼、特拉匹韦、他克莫司、泊沙康唑、依伐卡托、雷迪帕韦、Suvorexant、Ombitasvir、paritaprevir、daclatasvir、卡利拉嗪、brexpiprazole、奥培米芬、左乙拉西坦、ivacaftor、eluxadoline、lumacaftor、ivacaftor、艾曲泊帕、尼达尼布、美洛昔康、吗啡、马西替坦、度他雄胺、阿比特龙、lumacaftor、达格列净、他司美琼、依鲁替尼、帕拉米韦、奥拉帕尼、依帕列净、idelalisib、贝利司他、色瑞替尼、阿普斯特、泊马度胺、奥培米芬、卡格列净、甲磺酸达拉非尼、曲美替尼、dolutegravir、vortioxetine、bazedoxifene、simeprevir、阿西替尼、Vismodegib、阿伐那非、氯卡色林、米拉贝隆、博舒替尼、特立氟胺、Regorafenib、托法替尼、Cabozantinib、帕纳替尼、阿哌沙班、Bedaquiline、Crofelemer、波塞普韦、特拉普韦、贝拉赛普、维拉芬尼、克唑替尼、罗氟司特、维拉唑酮、阿梓沙坦、加巴喷丁、范德他尼、那格列汀、利匹韦林、非达霉素、依佐加滨、醋酸艾替班特、利伐沙班、替卡格雷、polidocanol、carglumic acid、替莫瑞林、vemurafenib、cabazitaxel、达比加群酯、依维莫司、托伐普坦、prasugrel、saxagliptin、telavancin、pazopanib、silodosin、rufinamide、艾曲波帕、乙酰唑胺、对乙酰氨基酚、阿昔洛韦、阿托伐他汀、阿托伐他汀钙、安普那韦、阿立哌唑、阿替洛尔、氯胺酮、阿托喹酮、咪唑硫嘌呤、阿奇霉素、布地奈德、骨化三醇、异丙基甲丁双脲、头孢地尼、头孢克肟、乙酸头孢呋辛、塞来昔布、头孢氨苄、氯噻嗪、克拉霉素、氯吡格雷硫酸氢盐、克霉唑、倍他米松、二氨二苯酚、双氯芬酸钠、双环胺、抵达诺新、曲大麻酚、度洛西汀、度他雄胺、依托度酸、依泽替米贝、辛伐他汀、非尔氨酯、非诺贝特、氟卡尼、膦沙那韦、呋喃苯胺酸、二甲苯氧庚酸、格列美脲、格列本脲、灰黄霉素、布洛芬、羟化氯喹、羟嗪、吲哚美辛、厄贝沙坦、异烟肼、依拉地平、酮康唑、拉莫三嗪、兰索拉唑、拉坦前列素、利奈唑胺、洛派丁胺、氯碳头孢、氯雷他定、洛伐他汀、甲苯咪唑、氯苯甲嗪、巯嘌呤、氨水杨酸、美他沙酮、苯哌啶醋酸甲酯、甲基强的松龙、莫达非尼、麦考酚酸、麦考酚酸酯、纳布美通、萘普生、硝苯地平、奥美拉唑、卡马西平、 盐酸羟考酮、非那吡啶、苯妥英钠、吡格列酮盐酸盐、吡罗昔康、去氧苯巴比妥、丙氯拉嗪、黄体酮、乙胺嘧啶、奎硫平、雷洛昔芬盐酸盐、利福布汀、利福平、利培酮、螺内酯、磺胺甲恶唑、他达拉非、替米沙坦、替拉那韦、缬沙坦、伐地那非、齐拉西酮、硫酸阿巴卡韦、可待因、沙丁胺醇、阿仑膦酸钠、别嘌醇、克拉维酸钾、苯甲托品、比马前列素、丁苯诺啡、纳洛酮、卡托普利、左旋多巴、头孢克肟、头孢羟氨苄、西替利嗪盐酸盐、环丙沙星、秋水仙碱、麦角钙化醇、法莫替丁、伪麻黄碱、叶酸、加巴喷丁、肼苯哒嗪、氢氯噻嗪、沙丁胺醇、左西替利、左氧氟沙星、左甲状腺素钠、赖诺普利、氨甲喋呤、甲基多巴、纳多洛尔、制霉菌素、泮托拉唑、磷酸伯氨喹、吡嗪酰胺、雷尼替丁盐酸盐、利巴韦林、利塞膦酸钠、索利那新、安体舒通、舒马曲普坦琥珀酸盐、特拉唑嗪、四环素、硫胺素、托吡酯、伐昔洛韦盐酸盐、缬更昔洛韦、阿卡波糖、醋氯芬酸、乙酰唑胺、乙酰肉毒碱、阿苯达唑、烯丙柳胺醇、阿米洛利、阿托品、硫唑嘌呤、阿奇霉素、贝尼地平、苄丝肼、苄硝唑、比卡鲁胺、比沙可啶、卡麦角林、坎地沙坦、卡培他滨、卡维地洛、头孢托仑、头孢美唑、头孢替安、头孢泊肟、头孢他啶、头孢呋辛酯、塞来考昔、氯霉素、氯丙嗪、西拉普利、西洛他唑、西咪替丁、西酞普兰、氯苯吩嗪、环孢素、环丙孕酮、氨苯砜、乙胺嗪、地高辛、二氯尼特、脱氧氟尿苷、强力霉素、依巴斯汀、依法韦仑、依帕司他、普沙坦、红霉素、乙胺丁醇、依泽替米贝、泛昔洛韦、非诺贝特、氟康唑、氟比洛芬、利尿磺胺、呋喃硫胺、吉非替尼、格列齐特、格列吡嗪、灰黄霉素、氟哌啶醇、盐酸羟嗪、布洛芬、伊马替尼、咪达普利、茚地那韦、厄贝沙坦、异烟肼、伊维菌素、酮洛芬、拉莫三嗪、左氧氟沙星、洛匹那韦、乐伐他汀、马尼地平、甲苯咪唑、甲羟孕酮、氨基水杨酸、美他沙酮、甲氨蝶呤、甲基多巴、甲硝唑、莫达非尼、莫沙必利、萘丁美酮、萘啶酸、奈非那韦、新斯的明、奈韦拉平、尼可地尔、烟酰胺、硝呋莫司、尼伐地平、尼美舒利、唑吡坦、佐米曲普坦、扎托洛芬、华法林、伏格列波糖、维拉帕米、丙戊酸、熊去氧胆酸、曲美他嗪、妥舒沙星、噻氯匹定、茶碱、替普瑞酮、替诺福韦、替加氟、他莫昔芬、他替瑞林、舒他西林、舒必利、柳氮磺胺吡啶、磺胺甲恶唑、磺胺嘧啶、司他夫定、罗红霉素、罗非昔布、利扎曲普坦、利托那韦、利塞膦酸、利福平、利福昔明、瑞巴派特、雷尼替丁、雷贝拉唑、尼扎替丁、炔诺酮、奥氮平、奥洛他定、奥利司他、奥司他韦、奥卡西平、喹硫平、盐酸吡哆醇、溴吡斯、丙基硫氧嘧啶、丙卡特罗、吡喹酮、普鲁司特、苯妥英钠、苯巴比妥、苯甲曲秦、培哚普利、羟考酮、地塞米松、呋塞米。The controlled release pharmaceutical composition according to claim 18, wherein said BCSII to IV drugs are selected from the group consisting of febuxostat, ixazomib, Alectinib, Erismodegib, vandetanib, aprepitant, and volpa sulfate Sand, aspirin, metformin, nglipepsin, linagliptin, naltrexone, dasabuvir, sofosbuvir, amphetamine, etravirine, everolimus, itraconazole, verrofi Nitra, telaprevir, tacrolimus, posaconazole, isikato, radipavir, Suvorexant, Ombitasvir, paritaprevir, daclatasvir, cariprazine, brexpiprazole, olpemiprofen, leztra Seatan, ivacaftor, eluxadoline, lumacaftor, ivacaftor, ezeppa, nidanib, meloxicam, morphine, macitentan, dutasteride, abiraterone, lumacaftor, daglibine, he Simeiqiong, Ibrutinib, Paramivir, Olapani, Epalibene, Idelalisib, Bellistat, Coloritinib, Apster, Pomamide, Obepamine , calpagliflozin, darabifen mesylate, trimetinib, dolutegravir, vortioxetine, baz Edoxifene, simeprevir, axitinib, Vismodegib, avermectin, lorcaserin, mirabine, bosutinib, teriflamine, Regorafenib, tofacitinib, cabozantinib, panatinib, Apixaban, Bedaquiline, Crofelemer, Poseprevir, Trafivir, Bellacit, Verapamil, Crizotinib, Roflumilast, Verazodone, Azurtan, Gabapentin , vandetanib, nategliptin, rivivirin, fidarimycin, ezazobine, icatibine acetate, rivaroxaban, ticagrelor, polidocanol, carglumic acid, temoline , vemurafenib, cabazitaxel, dabigatran etexilate, everolimus, tolvaptan, prasugrel, saxagliptin, telavancin, pazopanib, silodosin, rufinamide, eltrombopag, acetazolamide, acetaminophen, acyclovir Wei, atorvastatin, atorvastatin calcium, amprenavir, aripiprazole, atenolol, ketamine, ataquinone, azathioprine, azithromycin, budesonide, calcitriol, Isopropyl methylbutazone, cefdinir, cefixime, cefofurate , celecoxib, cephalexin, chlorothiazide, clarithromycin, clopidogrel hydrogen sulphate, clotrimazole, betamethasone, diaminodiphenol, diclofenac sodium, bicyclic amine, arrived in Nuoxin, cannabinol , duloxetine, dutasteride, etodolac, ezetimibe, simvastatin, felamine, fenofibrate, flecainide, phosphaviravir, furosemide, xylene Oxyheptanoic acid, glimepiride, glibenclamide, griseofulvin, ibuprofen, hydroxychloroquine, hydroxyzine, indomethacin, irbesartan, isoniazid, irilappine, ketocon Azole, lamotrigine, lansoprazole, latanoprost, linezolid, loperamide, chlorocarbon cephalosporin, loratadine, lovastatin, mebendazole, meclizine, guanidine, Ammonia salicylic acid, metaxalone, methylphenidate methyl acetate, methylprednisolone, modafinil, mycophenolic acid, mycophenolate mofetil, nabumetone, naproxen, nifedipine Dipine, omeprazole, carbamazepine, oxycodone hydrochloride, phenazopyridine, phenytoin, pioglitazone hydrochloride, piroxicam, deoxyphenobarbital, prochlorperazine Progesterone, pyrimethamine, quetiapine, raloxifene hydrochloride, rifabutin, rifampicin, risperidone, spironolactone, sulfamethoxazole, tadalafil, telmisartan, Ranavir, valsartan, vardenafil, ziprasidone, abacavir sulfate, codeine, salbutamol, alendronate, allopurinol, potassium clavulanate, benzotropine, Bimatoprost, buprenorphine, naloxone, captopril, levodopa, cefixime, cefadroxil, cetirizine hydrochloride, ciprofloxacin, colchicine, ergot calcification Alcohol, famotidine, pseudoephedrine, folic acid, gabapentin, hydralazine, hydrochlorothiazide, albuterol, levocetirizine, levofloxacin, levothyroxine sodium, lisinopril, methotrexate, methyldopa, nadolol , nystatin, pantoprazole, primaquine phosphate, pyrazinamide, ranitidine hydrochloride, ribavirin, risedronate sodium, solifenacin, spironolactone, suma Triptan succinate, terazosin, tetracycline, thiamine, topiramate, valacyclovir hydrochloride, valganciclovir, ar Carbohydrate, aceclofenac, acetazolamide, acetylcarnitine, albendazole, allenamide, amiloride, atropine, azathioprine, azithromycin, benidipine, benserazide, Benzidazole, bicalutamide, bisacodyl, cabergoline, candesartan, capecitabine, carvedilol, cefditoren, cefmetazole, cefotiam, cefpodoxime, ceftazidime, Cefuroxime axetil, celecoxib, chloramphenicol, chlorpromazine, cilazapril, cilostazol, cimetidine, citalopram, chlorpheniramine, cyclosporine, cyproterone , dapsone, ethamazine, digoxin, dichlorit, deoxyfluorouridine, doxycycline, ebastine, efavirenz, epalrestat, valsartan, erythromycin, B Aminobutanol, ezetimibe, famciclovir, fenofibrate, fluconazole, flurbiprofen, diurea, furosemide, gefitinib, gliclazide, glipizide, gray yellow Neomycin, haloperidol, hydroxyzine hydrochloride, ibuprofen, imatinib, midazolam, indinavir, irbesartan, isoniazid, ivermectin, ketoprofen, pull Motriazine Levofloxacin, lopinavir, levastatin, manidipine, mebendazole, medroxyprogesterone, aminosalicylic acid, metaxalone, methotrexate, methyldopa, metronidazole, modafi Nis, mosapride, nabumetone, nalidixic acid, nelfinavir, neostigmine, nevirapine, nicorandil, nicotinamide, nifuroxime, nilvadipine, nimesulide, Zolpidem, zolmitriptan, zaltoprofen, warfarin, voglibose, verapamil, valproic acid, ursodeoxycholic acid, trimetazidine, tosufloxacin, Ticlopidine, theophylline, teprenone, tenofovir, tegafur, tamoxifen, statin, sultamicill, sulpiride, sulfasalazine, sulfamethoxazole, sulfadiazine , stavudine, roxithromycin, rofecoxib, rizatriptan, ritonavir, risedronate, rifampicin, rifaximin, rebamipide, ranitidine , rabeprazole, nizatidine, norethisterone, olanzapine, olopatadine, orlistat, oseltamivir, oxcarbazepine, quetiapine, pyridoxine hydrochloride, bromide Propyl thiouracil, Procaterol, praziquantel, pranlukast, phenytoin, phenobarbital, phendimetrazine, perindopril, oxycodone, dexamethasone, furosemide.
  20. 根据权利要求1-8任一项所述的控释药物组合物,其特征在于所述延迟释放漂浮组分还还包含至少一种塑化剂,所述塑化剂选自枸橼酸三乙酯、枸橼酸三丁酯、聚乙二 醇、邻苯二甲酸三乙酯、邻苯二甲酸三丁酯、癸二酸二丁酯、癸二酸二乙酯、硬脂酸甘油酯、丁二酸二乙酯、丙二醇、蓖麻油和三乙酸甘油酯,优选枸橼酸三乙酯,所述增塑剂的含量为0.01%-50%,优选0.1-30%,最优选2.5%-15%(质量百分比,以固体组分的总质量为100计算)。The controlled release pharmaceutical composition according to any one of claims 1 to 8, wherein the delayed release floating component further comprises at least one plasticizer selected from the group consisting of triethyl citrate Ester, tributyl phthalate, polyethylene glycol, triethyl phthalate, tributyl phthalate, dibutyl sebacate, diethyl sebacate, glyceryl stearate, Diethyl succinate, propylene glycol, castor oil and triacetin, preferably triethyl citrate, the plasticizer is present in an amount of from 0.01% to 50%, preferably from 0.1% to 30%, most preferably 2.5%. 15% (mass percent, calculated as the total mass of the solid components is 100).
  21. 根据权利要求1-8任一项所述的控释药物组合物,其特征在于所述速释组分和/或延迟释放漂浮组分还包含至少一种药学上可接受的其他赋形剂。The controlled release pharmaceutical composition according to any one of claims 1 to 8, characterized in that the immediate release component and/or the delayed release floating component further comprises at least one pharmaceutically acceptable other excipient.
  22. 根据权利要求21所述的控释药物组合物,其特征在于所述赋形剂选自填充剂、润滑剂、粘合剂、崩解剂。The controlled release pharmaceutical composition according to claim 21, wherein the excipient is selected from the group consisting of a filler, a lubricant, a binder, and a disintegrant.
  23. 根据权利要求1-8任一项所述的控释药物组合物,其为片剂或胶囊。A controlled release pharmaceutical composition according to any one of claims 1-8 which is a tablet or capsule.
  24. 根据权利要求1-8任一项所述的控释药物组合物,其特征在于所述速释组分中的活性药物与延迟释放组分中的活性药物相同或者不同,优选相同。The controlled release pharmaceutical composition according to any one of claims 1 to 8, characterized in that the active drug in the immediate release component is the same as or different from the active drug in the delayed release component, preferably the same.
  25. 根据权利要求1-8任一项所述的控释药物组合物,其特征在于所述延迟释放漂浮组分中的活性药物在热熔挤出后任选保持晶型状态或者转变为无定型。The controlled release pharmaceutical composition according to any one of claims 1 to 8, characterized in that the active drug in the delayed release floating component is optionally maintained in a crystalline state or converted to an amorphous form after hot melt extrusion.
  26. 一种权利要求2-7任一项所述的控释药物组合物的制备方法,其特征在于包含以下步骤,1)在热熔挤出前将至少一种溶剂、延迟释放漂浮组分中活性成分和至少一种肠溶性聚合物混合得预混粗品或者热熔挤出过程中在线将至少一种溶剂、延迟释放漂浮组分中活性成分和至少一种肠溶性聚合物混合得预混粗品;2)预混粗品通过挤出机的加热螺杆区后经口模离开得挤出物。A method for preparing a controlled release pharmaceutical composition according to any one of claims 2 to 7, which comprises the steps of: 1) reacting at least one solvent, delayed release floating component before hot melt extrusion Mixing the ingredients with at least one enteric polymer to obtain a premixed crude product or mixing the at least one solvent, the active ingredient in the delayed release floating component, and the at least one enteric polymer in a hot melt extrusion process to obtain a premixed crude product; 2) The premixed crude product passes through the heating screw zone of the extruder and exits the extrudate through the die.
  27. 根据权利要求27所述的制备方法,其特征在于所述溶剂优选沸点在30-110℃之间的溶剂。The production method according to claim 27, wherein the solvent is preferably a solvent having a boiling point between 30 and 110 °C.
  28. 根据权利要求28所述的制备方法,其特征在于所述溶剂选自水、甲醇、乙醇、异丙醇、丙酮、戊烷、己烷、庚烷、环己烷、二氯甲烷、四氢呋喃,优选水、乙醇。The preparation method according to claim 28, wherein the solvent is selected from the group consisting of water, methanol, ethanol, isopropanol, acetone, pentane, hexane, heptane, cyclohexane, dichloromethane, tetrahydrofuran, preferably Water, ethanol.
  29. 根据权利要求28所述的制备方法,其特征在于所述溶剂的用量为0.1%-70%,优选1%-50%,最优选10%-30%(质量百分比,以固体组分的总质量为100计算)。The process according to claim 28, wherein the solvent is used in an amount of from 0.1% to 70%, preferably from 1% to 50%, most preferably from 10% to 30% by mass based on the total mass of the solid component. Calculated for 100).
  30. 根据权利要求26所述的制备方法,其特征在于口模温度为70-200℃,优选90-180℃,更优选110-160℃。The process according to claim 26, wherein the die temperature is from 70 to 200 ° C, preferably from 90 to 180 ° C, more preferably from 110 to 160 ° C.
  31. 根据权利要求30所述的制备方法,其特征在于溶剂注入螺杆区温度为10-90℃。The method according to claim 30, wherein the temperature of the solvent injection screw zone is from 10 to 90 °C.
  32. 根据权利要求26-31所述的制备方法,其特征在于还包含任选以下的步骤:1)将挤出物冷却;2)将挤出物去溶剂;3)将挤出物切割。The method of preparation according to claims 26-31, further comprising the step of: 1) cooling the extrudate; 2) removing the extrudate from the solvent; 3) cutting the extrudate.
  33. 根据权利要求26-31任一项所述的制备方法,其特征在于所述挤出机选自单螺杆热熔挤出机、啮合螺杆挤出机、双螺杆热熔挤出机,优选双螺杆热熔挤出机。The preparation method according to any one of claims 26 to 31, characterized in that the extruder is selected from the group consisting of a single screw hot melt extruder, an intermeshing screw extruder, a twin screw hot melt extruder, preferably a twin screw Hot melt extruder.
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