EP4308106A1 - Microsphere formulations comprising naltrexone and methods for making and using the same - Google Patents

Microsphere formulations comprising naltrexone and methods for making and using the same

Info

Publication number
EP4308106A1
EP4308106A1 EP22772358.2A EP22772358A EP4308106A1 EP 4308106 A1 EP4308106 A1 EP 4308106A1 EP 22772358 A EP22772358 A EP 22772358A EP 4308106 A1 EP4308106 A1 EP 4308106A1
Authority
EP
European Patent Office
Prior art keywords
polymer
microsphere
teg
naltrexone
ethylene glycol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP22772358.2A
Other languages
German (de)
French (fr)
Inventor
Bradley MINROVIC
Emma STRAIGHT
Kaitlin ZEMANSKI
Tracy RICHEY
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Oakwood Laboratories LLC
Original Assignee
Oakwood Laboratories LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Oakwood Laboratories LLC filed Critical Oakwood Laboratories LLC
Publication of EP4308106A1 publication Critical patent/EP4308106A1/en
Pending legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/435Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with one nitrogen as the only ring hetero atom
    • A61K31/47Quinolines; Isoquinolines
    • A61K31/485Morphinan derivatives, e.g. morphine, codeine
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/30Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
    • A61K47/36Polysaccharides; Derivatives thereof, e.g. gums, starch, alginate, dextrin, hyaluronic acid, chitosan, inulin, agar or pectin
    • A61K47/38Cellulose; Derivatives thereof
    • 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
    • A61K9/0019Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/06Ointments; Bases therefor; Other semi-solid forms, e.g. creams, sticks, gels
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/10Dispersions; Emulsions
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1629Organic macromolecular compounds
    • A61K9/1641Organic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyethylene glycol, poloxamers
    • A61K9/1647Polyesters, e.g. poly(lactide-co-glycolide)
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/19Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles lyophilised, i.e. freeze-dried, solutions or dispersions

Definitions

  • Naltrexone (chemical formula C20H23NO4; CAS Number 16590-41-3), characterized by the general structure: is a medication used to treat alcohol and opioid dependence. Naltrexone is currently orally administered as a tablet or injected into a muscle (commercially available under the trade name Vivitrol®).
  • Vivitrol® is a once-per-month extended-release microsphere formulation wherein naltrexone is encapsulated in a poly(D,L-lactide-co-glycolide), 75:25 polymer matrix, having a drug load of approximately 33.7% and a particle size of approximately 81 mih (D50). Vivitrol® must not be administered intravenously or subcutaneously. Some patients experience side effects from using Vivitrol® and may require another treatment option.
  • naltrexone-encapsulating microsphere formulation especially one having a high drug load (> ⁇ 45 % by weight), small particle size (about 25-55 mih (D50)), long release duration (> ⁇ 30, 60, or even 90 days), and a different mode of release.
  • Microsphere formulations comprising naltrexone are provided.
  • the microsphere formulations comprise polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising either a poly(ortho ester) polymer (a “POE”) or a poly(D,L-lactide) polymer (a “PLA”), wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), with the proviso that the biodegradable polymer does not include a poly (D,L-lactide-co-glycolide) (a “PLGA”).
  • PEO poly(ortho ester) polymer
  • PLA poly(D,L-lactide) polymer
  • the microsphere formulations are characterized in that the naltrexone is released over a period of about 90 days (i.e., 90 days). In other aspects, the microsphere formulations are characterized in that the naltrexone is released over a period of about 30 days (i.e., ⁇ 10% of 30 days) or about 60 days (i.e., ⁇ 10% of 60 days). In another aspect, the microsphere formulations are characterized in that they have a low initial burst release, that is, not more than 20% of the naltrexone is released within about 24 hours of injection into a subject.
  • the microsphere formulations may be made by a method, the method comprising: (A) mixing: (i) the biodegradable polymer comprising a POE or a PLA; (ii) a primary solvent; (iii) naltrexone; and (iv) a co-solvent, to form a dispersed phase; (B) mixing: (i) water; and (ii) a surfactant, to form a continuous phase; and (C) combining the dispersed phase with the continuous phase in a homogenizer.
  • a method for treating alcohol and/or opioid dependence may comprise administering by intramuscular or subcutaneous injection to a patient in need thereof a microsphere formulation made according to the methods described herein, wherein the formulation is administered to the patient with a dosing schedule of about every 30, 60, or 90 days.
  • a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), in the manufacture of a medicament for the treatment of alcohol and/or opioid dependence.
  • a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), is provided for use as a medicament for the treatment of alcohol and/or opioid dependence.
  • kits comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso).
  • Figure 1 is a schematic depicting a method for making naltrexone-encapsulated polymer microspheres.
  • Figure 2 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating PLA-based polymer microspheres in direct comparison to Vivitrol®.
  • Figure 3 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating POE-based polymer microspheres in direct comparison to Vivitrol®.
  • Microsphere formulations comprising naltrexone are provided.
  • the microsphere formulations comprise polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso).
  • the microsphere formulations may be made by a method, the method comprising: (A) mixing: (i) the biodegradable polymer comprising a POE or a PLA, but not a PLGA; (ii) a primary solvent; (iii) naltrexone; and (iv) a co-solvent, to form a dispersed phase; (B) mixing: (i) water; and (ii) a surfactant, to form a continuous phase; and (C) combining the dispersed phase with the continuous phase in a homogenizer.
  • the naltrexone is a free base supplied by Mallinckrodt Pharmaceuticals.
  • the naltrexone has a di chi orom ethane (“DCM”) solubility of 100 mg/mL, ethyl acetate (“EA”) solubility of 26 mg/mL, and benzyl alcohol (“BA”) solubility of >250 mg/mL.
  • DCM di chi orom ethane
  • EA ethyl acetate
  • BA benzyl alcohol
  • the naltrexone is an HC1 salt supplied by Mallinckrodt Pharmaceuticals.
  • the naltrexone HC1 salt has a water solubility of about 100 mg/mL.
  • the biodegradable polymer is a POE.
  • POEs release through surface degradation, as compared to PLGAs, which release by bulk hydrolysis.
  • Suitable POE polymers or co-polymers may include a cyclohexanedimethanoktriethylene glycol (CHDM:TEG) co polymer, a cy cl ohexanedimethanoktri ethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri-block polymer, a 3,9-Diethylidene-2,4,8,10- tetraoxaspiro[5.5]undecane:triethylene glycol (DETOSU:TEG), or a 3,9-Diethylidene-2,4,8,10- tetraoxaspiro[5.5]undecane:triethylene glycol :tri ethylene glycol glycolide (DETOSU:TEG- GL).
  • CHDM:TEG cyclohex
  • the CHDM:TEG ratio may be about 93:7, with a molecular weight of about 22 kDa. In one aspect, the CHDM:TEG:TEG-GL ratio may be about 88:10:2, with a molecular weight of about 27 kDa. In another aspect, the CHDM:TEG:TEG-GL ratio may be about 70:0:30, with a molecular weight of about 20 kDa.
  • the biodegradable polymer is a PLA.
  • the PLA may have an inherent viscosity of about 0.15 dL/g to about 0.75 dL/g, including from about 0.15 dL/g to about 0.25 dL/g, from about 0.26 dL/g to about 0.54 dL/g, including 0.36 dL/g, and from about 0.55 dL/g to about 0.75 dL/g.
  • PLGA polymers are specifically excluded. Dispersed Phase
  • the dispersed phase comprises a primary solvent.
  • the primary solvent comprises DCM.
  • the dispersed phase may also include up to about 50% by weight of a co-solvent capable of optimizing the solubility of naltrexone in the dispersed phase.
  • the co-solvent may be BA, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, acetonitrile, ethanol, N-methyl pyrrolidone, EA, or any other solvent that increases the solubility of naltrexone in the dispersed phase.
  • the primary solvent comprises DCM
  • the co-solvent comprises BA.
  • the ratio of DCM to BA is about 3:1.
  • microspheres are considered to be “essentially free” of organic solvent if the microsphere meets the standards set forth in the “ICH Harmonised Guideline, Impurities: Guideline for Residual Solvents Q3C(R8), Current Step 4 version dated 22 April 2021,” which is incorporated herein by reference in its entirety.
  • the dispersed phase may be combined with an aqueous continuous phase that comprises water and, optionally, a surfactant.
  • the continuous phase has a pH of about 6.
  • the surfactant component may be present in the continuous phase in an amount of about 0.35% to about 1.0% by weight in water.
  • the surfactant component comprises polyvinyl alcohol (“PVA”) in a concentration of about 0.35% by weight in water.
  • the dispersed phase flow rate to the homogenizer may be from about 10 mL/min to about 30 mL/min, including about 20 mL/min and about 25 mL/min. In some aspects, the continuous phase flow rate to the homogenizer may be about 2L/min. Thus, in one aspect, the continuous phase: dispersed phase ratio may be from about 66:1 to about 200:1, including about 100:1 and about 80:1.
  • the continuous phase may be provided at room temperature or above or below room temperature. In some aspects, the continuous phase may be provided at about 40 °C, about 37 °C, about 35 °C, about 30 °C, about 25 °C, about 20 °C, about 15 °C, about 10 °C, about 5 °C, about 0 °C, and any range or value between any of those temperature values.
  • the phrase “homogenizer” contemplates a system or apparatus that can homogenize the dispersed phase and the continuous phase, emulsify the dispersed phase and the continuous phase, or both, which systems and apparatuses are known in the art.
  • the homogenizer is an in-line Silverson Homogenizer (commercially available from Silverson Machines, Waterside, UK) or a Levitronix® BPS-ilOO integrated pump system used, e.g., as described in U.S. Patent No. 11,167,256, which is incorporated by reference herein in its entirety.
  • the homogenizer is a membrane emulsifier.
  • the homogenizer runs at an impeller speed of about 1,000 to about 4,000 revolutions per minute (“RPM”), including about 1,250 RPM, about 2,000 RPM, about 3,250 RPM, or any value or range between any of those RPM values.
  • RPM revolutions per minute
  • the drug load of each polymer microsphere in a drug to polymer ratio may be about 45 wt/wt%, greater than 40 wt/wt%, about 50 wt/wt%, and from about
  • the polymer microspheres may be any size that is safely and efficaciously injectable.
  • the polymer microspheres may have an average particle size between about 25 mih (p5o) and about 55 mih (Dso), between about 25 mih (Dso) and about 35 mih (Dso), between about 35 mih (Dso) and about 45 mih (Dso), between about 45 mih (Dso) and about 55 mih (Dso), less than about 55 mih (Dso), and less than about 60 mih (Dso).
  • the microsphere formulations may be characterized in that they have a duration of release of at least about two weeks and up to about twelve weeks. In some aspects, the microsphere formulations have a duration of release of about three weeks, about four weeks, about five weeks, and about six weeks. In some aspects, the duration of release is about 30 days.
  • the microsphere formulations may be characterized in that they may have a duration of release of at least about 60 days.
  • the microsphere formulations may be characterized in that they have a duration of release of about 90 days.
  • microsphere formulations are further characterized in that they have a low initial burst release, that is, not more than 20% of the naltrexone is released within about 24 hours of injection into a subject.
  • a method for treating alcohol and/or opioid dependence may comprise administering by intramuscular or subcutaneous injection to a patient in need thereof a microsphere formulation made according to the methods described herein, wherein the formulation is administered to the patient with a dosing schedule of about every 30, 60, or 90 days.
  • a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), in the manufacture of a medicament for the treatment of alcohol and/or opioid dependence.
  • a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), is provided for use as a medicament for the treatment of alcohol and/or opioid dependence.
  • kits comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso).
  • Example 1 General preparation of polymer microspheres comprising naltrexone
  • a dispersed phase (“DP”) 10 is formed by dissolving a polymer matrix (such as a POE or PL A polymer) in an organic solvent system (such as DCM and BA), followed by the addition of naltrexone with mixing until completely dissolved.
  • the DP 10 is filtered using a 0.2 mih sterilizing PTFE or PVDF membrane filter (such as EMFLON, commercially available from Pall or SartoriousAG) and pumped into a homogenizer 30 at a defined flow rate.
  • a continuous phase (“CP”) 20 comprising water and surfactant is also pumped into the homogenizer 30 at a defined flow rate.
  • the speed of the homogenizer 30 is generally fixed to achieve a desired polymer microsphere size distribution.
  • a representative continuous “upstream” microsphere formation phase is described in U.S. Pat. No. 5,945,126, which is incorporated by reference herein in its entirety.
  • Microsphere Processing Phase The formed or forming microspheres exit the homogenizer 30 and enter a solvent removal vessel (“SRV”) 40. Water may be added to the SRV 40 during microsphere formation to minimize the solvent level in the aqueous medium. See, e.g., U.S. Patent No. 9,017,715, which is incorporated by reference herein in its entirety.
  • SRV solvent removal vessel
  • Solvent removal is achieved using water washing and a hollow fiber filter (commercially available as HFF from Cytiva) 50.
  • a representative “downstream” microsphere processing phase is described in U.S. Pat. No. 6,270,802, which is incorporated by reference herein in its entirety.
  • Example 2 Preparation of Naltrexone-Encapsulated PLA Polymer Microspheres - Batch 1 [0039] Following the general procedure described in Example 1, illustrated in Figure 1, and detailed in Table 1, the DP was formed by dissolving 13.5 g of DL-PLA polymer in 59.4 g of DCM and 19.8 g of BA (DCM/BA (3 : 1)), followed by addition of naltrexone (16.5 g) with mixing until completely dissolved.
  • the DP was filtered and pumped at a flow rate of 25 mL/min into a Levitronix® BPS-ilOO integrated pump system operating at 3,250 RPM.
  • the formed or forming microspheres exited the homogenizer and entered the SRV.
  • Deionized water was added to the SRV. Solvent removal was achieved using water washing and a hollow fiber filter.
  • the bulk suspension was collected via filtration and lyophilized to obtain a free-flowing powder.
  • Figure 2 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating PLA polymer microspheres in direct comparison to Vivitrol®.
  • the formed or forming microspheres exited the homogenizer and entered the SRV.
  • Deionized water was added to the SRV.
  • Solvent removal was achieved using water washing and a hollow fiber filter.
  • the bulk suspension was collected via filtration and lyophilized to obtain a free-flowing powder.
  • FIG. 1 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating POE polymer microspheres in direct comparison to Vivitrol®.
  • the formed or forming microspheres exited the homogenizer and entered the SRV.
  • Deionized water was added to the SRV.
  • Solvent removal was achieved using water washing and a hollow fiber filter.
  • the bulk suspension was collected via filtration and lyophilized to obtain a free-flowing powder.
  • microsphere suspension was dosed with 2% ethanol by volume and stirred for one hour. After stirring, the dosed microsphere suspension was concentrated and subjected to normal washing steps. This is intended to decrease the initial burst of the microspheres in vivo.
  • the microspheres may be suspended in a diluent for administration (injection).
  • the diluent may generally contain a thickening agent, a tonicity agent, and a surfactant.
  • the thickening agent may include carboxymethyl cellulose-sodium (CMC-Na) or other suitable compounds.
  • CMC-Na carboxymethyl cellulose-sodium
  • An appropriate viscosity grade and suitable concentration of CMC-Na may be selected so that the viscosity of the diluent is 3 cps or higher.
  • a viscosity of about 10 cps is suitable; however, a higher viscosity diluent may be preferred for larger microspheres in order to minimize the settling of microspheres in the suspension.
  • each it is not meant to mean “each and every, without exception.”
  • microsphere formulation comprising polymer microspheres, and “each polymer microsphere” is said to have a particular API content, if there are 10 polymer microspheres, and two or more of the polymer microspheres have the particular API content, then that subset of two or more polymer microspheres is intended to meet the limitation.

Landscapes

  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Epidemiology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • Veterinary Medicine (AREA)
  • Medicinal Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Emergency Medicine (AREA)
  • Dermatology (AREA)
  • Dispersion Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Medicinal Preparation (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

Microsphere formulations comprising naltrexone are provided. The microsphere formulations comprise polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mm to about 55 mm (D50). Methods for making and using the microsphere formulations are also provided.

Description

MICROSPHERE FORMULATIONS COMPRISING NALTREXONE AND METHODS FOR MAKING AND USING THE SAME
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application claims priority from U.S. Provisional Patent Application No.
63/266,660, filed on January 11, 2022, U.S. Provisional Patent Application No. 63/161,159, filed on March 15, 2021, and U.S. Provisional Patent Application No. 63/161,187, filed on March 15,
2021, each of which is incorporated by reference herein in its entirety.
BACKGROUND
[0002] Naltrexone (chemical formula C20H23NO4; CAS Number 16590-41-3), characterized by the general structure: is a medication used to treat alcohol and opioid dependence. Naltrexone is currently orally administered as a tablet or injected into a muscle (commercially available under the trade name Vivitrol®).
[0003] Vivitrol® is a once-per-month extended-release microsphere formulation wherein naltrexone is encapsulated in a poly(D,L-lactide-co-glycolide), 75:25 polymer matrix, having a drug load of approximately 33.7% and a particle size of approximately 81 mih (D50). Vivitrol® must not be administered intravenously or subcutaneously. Some patients experience side effects from using Vivitrol® and may require another treatment option. Thus, a need exists for an alternative extended-release naltrexone-encapsulating microsphere formulation, especially one having a high drug load (>~45 % by weight), small particle size (about 25-55 mih (D50)), long release duration (>~30, 60, or even 90 days), and a different mode of release.
SUMMARY
[0004] Microsphere formulations comprising naltrexone are provided. The microsphere formulations comprise polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising either a poly(ortho ester) polymer (a “POE”) or a poly(D,L-lactide) polymer (a “PLA”), wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), with the proviso that the biodegradable polymer does not include a poly (D,L-lactide-co-glycolide) (a “PLGA”). In one aspect, the microsphere formulations are characterized in that the naltrexone is released over a period of about 90 days (i.e., 90 days). In other aspects, the microsphere formulations are characterized in that the naltrexone is released over a period of about 30 days (i.e., ±10% of 30 days) or about 60 days (i.e., ±10% of 60 days). In another aspect, the microsphere formulations are characterized in that they have a low initial burst release, that is, not more than 20% of the naltrexone is released within about 24 hours of injection into a subject.
[0005] In one aspect, the microsphere formulations may be made by a method, the method comprising: (A) mixing: (i) the biodegradable polymer comprising a POE or a PLA; (ii) a primary solvent; (iii) naltrexone; and (iv) a co-solvent, to form a dispersed phase; (B) mixing: (i) water; and (ii) a surfactant, to form a continuous phase; and (C) combining the dispersed phase with the continuous phase in a homogenizer.
[0006] In one aspect, a method for treating alcohol and/or opioid dependence is provided. The method may comprise administering by intramuscular or subcutaneous injection to a patient in need thereof a microsphere formulation made according to the methods described herein, wherein the formulation is administered to the patient with a dosing schedule of about every 30, 60, or 90 days.
[0007] In another aspect, use is disclosed of a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), in the manufacture of a medicament for the treatment of alcohol and/or opioid dependence.
[0008] In another aspect, a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), is provided for use as a medicament for the treatment of alcohol and/or opioid dependence.
[0009] In another aspect, a kit is provided, the kit comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso). BRIEF DESCRIPTION OF THE FIGURES
[0010] Figure 1 is a schematic depicting a method for making naltrexone-encapsulated polymer microspheres.
[0011] Figure 2 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating PLA-based polymer microspheres in direct comparison to Vivitrol®.
[0012] Figure 3 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating POE-based polymer microspheres in direct comparison to Vivitrol®.
DETAILED DESCRIPTION
[0013] Microsphere formulations comprising naltrexone are provided. The microsphere formulations comprise polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso).
[0014] In one aspect, the microsphere formulations may be made by a method, the method comprising: (A) mixing: (i) the biodegradable polymer comprising a POE or a PLA, but not a PLGA; (ii) a primary solvent; (iii) naltrexone; and (iv) a co-solvent, to form a dispersed phase; (B) mixing: (i) water; and (ii) a surfactant, to form a continuous phase; and (C) combining the dispersed phase with the continuous phase in a homogenizer.
Naltrexone
[0015] In one aspect, the naltrexone is a free base supplied by Mallinckrodt Pharmaceuticals. In one aspect, the naltrexone has a di chi orom ethane (“DCM”) solubility of 100 mg/mL, ethyl acetate (“EA”) solubility of 26 mg/mL, and benzyl alcohol (“BA”) solubility of >250 mg/mL. In one aspect, the naltrexone has a pKa = 8.4.
[0016] In another aspect, the naltrexone is an HC1 salt supplied by Mallinckrodt Pharmaceuticals. In one aspect, the naltrexone HC1 salt has a water solubility of about 100 mg/mL.
Biodegradable Polymers
[0017] In one aspect, the biodegradable polymer is a POE. POEs release through surface degradation, as compared to PLGAs, which release by bulk hydrolysis. Suitable POE polymers or co-polymers may include a cyclohexanedimethanoktriethylene glycol (CHDM:TEG) co polymer, a cy cl ohexanedimethanoktri ethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri-block polymer, a 3,9-Diethylidene-2,4,8,10- tetraoxaspiro[5.5]undecane:triethylene glycol (DETOSU:TEG), or a 3,9-Diethylidene-2,4,8,10- tetraoxaspiro[5.5]undecane:triethylene glycol :tri ethylene glycol glycolide (DETOSU:TEG:TEG- GL). In one aspect, the CHDM:TEG ratio may be about 93:7, with a molecular weight of about 22 kDa. In one aspect, the CHDM:TEG:TEG-GL ratio may be about 88:10:2, with a molecular weight of about 27 kDa. In another aspect, the CHDM:TEG:TEG-GL ratio may be about 70:0:30, with a molecular weight of about 20 kDa.
[0018] In one aspect, the biodegradable polymer is a PLA. The PLA may have an inherent viscosity of about 0.15 dL/g to about 0.75 dL/g, including from about 0.15 dL/g to about 0.25 dL/g, from about 0.26 dL/g to about 0.54 dL/g, including 0.36 dL/g, and from about 0.55 dL/g to about 0.75 dL/g. In one aspect, the PLA comprises Lactel® DL-PLA, ester terminated, IV = 0.36 dL/g, MW = 46 kDa, supplied by Evonik Industries AG (“DL-PLA”).
[0019] In one aspect, PLGA polymers are specifically excluded. Dispersed Phase
[0020] In one aspect, the dispersed phase comprises a primary solvent. In one aspect, the primary solvent comprises DCM. The dispersed phase may also include up to about 50% by weight of a co-solvent capable of optimizing the solubility of naltrexone in the dispersed phase. In one aspect, the co-solvent may be BA, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, acetonitrile, ethanol, N-methyl pyrrolidone, EA, or any other solvent that increases the solubility of naltrexone in the dispersed phase. In one aspect, the primary solvent comprises DCM, and the co-solvent comprises BA. In one aspect, the ratio of DCM to BA is about 3:1. The organic solvent is removed from the microspheres in the course of their preparation. A microsphere is considered to be “essentially free” of organic solvent if the microsphere meets the standards set forth in the “ICH Harmonised Guideline, Impurities: Guideline for Residual Solvents Q3C(R8), Current Step 4 version dated 22 April 2021,” which is incorporated herein by reference in its entirety.
Continuous Phase
[0021] The dispersed phase may be combined with an aqueous continuous phase that comprises water and, optionally, a surfactant. In one aspect, the continuous phase has a pH of about 6.
[0022] The surfactant component may be present in the continuous phase in an amount of about 0.35% to about 1.0% by weight in water. In one aspect, the surfactant component comprises polyvinyl alcohol (“PVA”) in a concentration of about 0.35% by weight in water.
[0023] In some aspects, the dispersed phase flow rate to the homogenizer may be from about 10 mL/min to about 30 mL/min, including about 20 mL/min and about 25 mL/min. In some aspects, the continuous phase flow rate to the homogenizer may be about 2L/min. Thus, in one aspect, the continuous phase: dispersed phase ratio may be from about 66:1 to about 200:1, including about 100:1 and about 80:1.
[0024] The continuous phase may be provided at room temperature or above or below room temperature. In some aspects, the continuous phase may be provided at about 40 °C, about 37 °C, about 35 °C, about 30 °C, about 25 °C, about 20 °C, about 15 °C, about 10 °C, about 5 °C, about 0 °C, and any range or value between any of those temperature values.
Homogenizer
[0025] For brevity, and because the methods are equally applicable to either, the phrase “homogenizer” contemplates a system or apparatus that can homogenize the dispersed phase and the continuous phase, emulsify the dispersed phase and the continuous phase, or both, which systems and apparatuses are known in the art. For example, in one aspect, the homogenizer is an in-line Silverson Homogenizer (commercially available from Silverson Machines, Waterside, UK) or a Levitronix® BPS-ilOO integrated pump system used, e.g., as described in U.S. Patent No. 11,167,256, which is incorporated by reference herein in its entirety. In one aspect, the homogenizer is a membrane emulsifier. In one aspect, the homogenizer runs at an impeller speed of about 1,000 to about 4,000 revolutions per minute (“RPM”), including about 1,250 RPM, about 2,000 RPM, about 3,250 RPM, or any value or range between any of those RPM values.
Drug Load
[0026] The drug load of each polymer microsphere in a drug to polymer ratio, expressed as a percentage, may be about 45 wt/wt%, greater than 40 wt/wt%, about 50 wt/wt%, and from about
45 wt/wt% to about 55 wt/wt%. Particle Size
[0027] The polymer microspheres may be any size that is safely and efficaciously injectable. In one aspect, the polymer microspheres may have an average particle size between about 25 mih (p5o) and about 55 mih (Dso), between about 25 mih (Dso) and about 35 mih (Dso), between about 35 mih (Dso) and about 45 mih (Dso), between about 45 mih (Dso) and about 55 mih (Dso), less than about 55 mih (Dso), and less than about 60 mih (Dso).
Extended Release
[0028] Where the polymer is a PLA, the microsphere formulations may be characterized in that they have a duration of release of at least about two weeks and up to about twelve weeks. In some aspects, the microsphere formulations have a duration of release of about three weeks, about four weeks, about five weeks, and about six weeks. In some aspects, the duration of release is about 30 days.
[0029] Where the polymer is a POE comprising CHDM:TEG with a ratio of about 93 :7, or the polymer is a POE comprising CHDM:TEG:TEG-GL with a ratio of about 88:10:2, the microsphere formulations may be characterized in that they may have a duration of release of at least about 60 days.
[0030] Where the polymer is a POE comprising CHDM:TEG:TEG-GL with a ratio of about 70:0:30, the microsphere formulations may be characterized in that they have a duration of release of about 90 days.
[0031] The microsphere formulations are further characterized in that they have a low initial burst release, that is, not more than 20% of the naltrexone is released within about 24 hours of injection into a subject. Therapeutic Benefits
[0032] In one aspect, a method for treating alcohol and/or opioid dependence is provided. The method may comprise administering by intramuscular or subcutaneous injection to a patient in need thereof a microsphere formulation made according to the methods described herein, wherein the formulation is administered to the patient with a dosing schedule of about every 30, 60, or 90 days.
[0033] In another aspect, use is disclosed of a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), in the manufacture of a medicament for the treatment of alcohol and/or opioid dependence.
[0034] In another aspect, a microsphere formulation comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso), is provided for use as a medicament for the treatment of alcohol and/or opioid dependence.
[0035] In another aspect, a kit is provided, the kit comprising polymer microspheres, each polymer microsphere comprising: (i) naltrexone; and (ii) a biodegradable polymer comprising a POE or a PLA, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of about 25 mih to about 55 mih (Dso). EXAMPLES
Example 1 - General preparation of polymer microspheres comprising naltrexone [0036] Microsphere Formation Phase. With reference to Figure 1, a dispersed phase (“DP”) 10 is formed by dissolving a polymer matrix (such as a POE or PL A polymer) in an organic solvent system (such as DCM and BA), followed by the addition of naltrexone with mixing until completely dissolved. The DP 10 is filtered using a 0.2 mih sterilizing PTFE or PVDF membrane filter (such as EMFLON, commercially available from Pall or SartoriousAG) and pumped into a homogenizer 30 at a defined flow rate. A continuous phase (“CP”) 20 comprising water and surfactant is also pumped into the homogenizer 30 at a defined flow rate. The speed of the homogenizer 30 is generally fixed to achieve a desired polymer microsphere size distribution. A representative continuous “upstream” microsphere formation phase is described in U.S. Pat. No. 5,945,126, which is incorporated by reference herein in its entirety.
[0037] Microsphere Processing Phase. The formed or forming microspheres exit the homogenizer 30 and enter a solvent removal vessel (“SRV”) 40. Water may be added to the SRV 40 during microsphere formation to minimize the solvent level in the aqueous medium. See, e.g., U.S. Patent No. 9,017,715, which is incorporated by reference herein in its entirety. After the DP 10 has been exhausted, the CP and water flow rates are stopped, and the washing steps are initiated. Solvent removal is achieved using water washing and a hollow fiber filter (commercially available as HFF from Cytiva) 50. A representative “downstream” microsphere processing phase is described in U.S. Pat. No. 6,270,802, which is incorporated by reference herein in its entirety. [0038] The washed microspheres are collected and freeze-dried overnight in a lyophilizer (Virtis) to remove any moisture. The resulting microspheres are a free-flowing off-white bulk powder. Example 2 - Preparation of Naltrexone-Encapsulated PLA Polymer Microspheres - Batch 1 [0039] Following the general procedure described in Example 1, illustrated in Figure 1, and detailed in Table 1, the DP was formed by dissolving 13.5 g of DL-PLA polymer in 59.4 g of DCM and 19.8 g of BA (DCM/BA (3 : 1)), followed by addition of naltrexone (16.5 g) with mixing until completely dissolved. The DP was filtered and pumped at a flow rate of 25 mL/min into a Levitronix® BPS-ilOO integrated pump system operating at 3,250 RPM. The CP comprising 0.35% PVA was also pumped into the homogenizer at a flow rate of 2 L/min (CP:DP = 80: 1). [0040] The formed or forming microspheres exited the homogenizer and entered the SRV. Deionized water was added to the SRV. Solvent removal was achieved using water washing and a hollow fiber filter. The bulk suspension was collected via filtration and lyophilized to obtain a free-flowing powder.
[0041] The process parameters and the characterization data for a representative batch (Batch #1) are shown in Table 1 in comparison to Vivitrol®:
Table 1
[0042] Figure 2 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating PLA polymer microspheres in direct comparison to Vivitrol®.
Example 3 - Preparation of Naltrexone-Encapsulated POE Polymer Microspheres - Batches 2-4 [0043] Following the general procedure described in Example 1, illustrated in Figure 1, and detailed in Table 2, the DP was formed by dissolving 13.5 g of POE in 59.4 g of DCM and 19.8 g of BA (DCM/BA (3 : 1)), followed by addition of naltrexone (16.5 g) with mixing until completely dissolved. The DP was filtered and pumped at a flow rate of 25 mL/min into a Levitronix® BPS- ilOO integrated pump system operating at 3,250 RPM (Batches 2 and 3) or 4,000 RPM (Batch 4). The CP comprising 0.35% PVA was also pumped into the homogenizer at a flow rate of 2 L/min (CP:DP = 80:1).
[0044] The formed or forming microspheres exited the homogenizer and entered the SRV. Deionized water was added to the SRV. Solvent removal was achieved using water washing and a hollow fiber filter. The bulk suspension was collected via filtration and lyophilized to obtain a free-flowing powder.
[0045] The process parameters and the characterization data for three representative batches (Batches 2-4) are shown in Table 2 in comparison to Vivitrol®: Table 2 [0046] Figure 3 is a graph showing naltrexone release over time in dogs from naltrexone- encapsulating POE polymer microspheres in direct comparison to Vivitrol®.
Example 4 - Preparation of Naltrexone-Encapsulated POE Polymer Microspheres - Batches 5-8 [0047] Following the general procedure described in Example 1, illustrated in Figure 1, and detailed in Table 3, the DP was formed by dissolving 13.5 g of POE in 59.4 g of DCM and 19.8 g of BA (DCM/BA (3 : 1)), followed by addition of naltrexone (16.5 g) with mixing until completely dissolved. The DP was filtered and pumped at a flow rate of 25 mL/min into a Levitronix® BPS- ilOO integrated pump system operating at 1,250 RPM (Batches 5 and 6) or 3,250 RPM (Batches 7 and 8). The CP comprising 0.35% PVA was also pumped into the homogenizer at a flow rate of 2 L/min (CP:DP = 80:1).
[0048] The formed or forming microspheres exited the homogenizer and entered the SRV. Deionized water was added to the SRV. Solvent removal was achieved using water washing and a hollow fiber filter. The bulk suspension was collected via filtration and lyophilized to obtain a free-flowing powder.
[0049] The process parameters and the characterization data for four representative batches (Batches 5-8) are shown in Table 3.
Table 3
* After the microsphere formation step, the microsphere suspension was dosed with 2% ethanol by volume and stirred for one hour. After stirring, the dosed microsphere suspension was concentrated and subjected to normal washing steps. This is intended to decrease the initial burst of the microspheres in vivo.
[0050] In use, the microspheres may be suspended in a diluent for administration (injection). The diluent may generally contain a thickening agent, a tonicity agent, and a surfactant. The thickening agent may include carboxymethyl cellulose-sodium (CMC-Na) or other suitable compounds. An appropriate viscosity grade and suitable concentration of CMC-Na may be selected so that the viscosity of the diluent is 3 cps or higher. Generally, a viscosity of about 10 cps is suitable; however, a higher viscosity diluent may be preferred for larger microspheres in order to minimize the settling of microspheres in the suspension. [0051] Uniform microsphere suspension without particle settling will result in a consistent delivered dose during drug administration by injection. To have a tonicity of the diluent closer to the biological system, about 290 milliosmole (mOsm), solutes such as mannitol, sodium chloride, or any other acceptable salt may be used.
[0052] The aspects disclosed herein are not intended to be exhaustive or to be limiting. A skilled artisan would acknowledge that other aspects or modifications to instant aspects can be made without departing from the spirit or scope of the invention. The aspects of the present disclosure, as generally described herein and illustrated in the figures, can be arranged, substituted, combined, separated, and designed in a wide variety of different configurations, all of which are contemplated herein.
[0053] Unless otherwise specified, “a,” “an,” “the,” “one or more of,” and “at least one” are used interchangeably. The singular forms “a”, “an,” and “the” are inclusive of their plural forms. The recitations of numerical ranges by endpoints include all numbers subsumed within that range (e.g., 1 to 5 includes 1, 1.5, 2, 2.75, 3, 3.80, 4, 5, etc.). The terms “comprising” and “including” are intended to be equivalent and open-ended. The phrase “consisting essentially of’ means that the composition or method may include additional ingredients and/or steps, but only if the additional ingredients and/or steps do not materially alter the basic and novel characteristics of the claimed composition or method. The phrase “selected from the group consisting of’ is meant to include mixtures of the listed group.
[0054] When reference is made to the term “each,” it is not meant to mean “each and every, without exception.” For example, if reference is made to microsphere formulation comprising polymer microspheres, and “each polymer microsphere” is said to have a particular API content, if there are 10 polymer microspheres, and two or more of the polymer microspheres have the particular API content, then that subset of two or more polymer microspheres is intended to meet the limitation.
[0055] The term “about” in conjunction with a number is simply shorthand and is intended to include ±10% of the number. This is true whether “about” is modifying a stand-alone number or modifying a number at either or both ends of a range of numbers. In other words, “about 10” means from 9 to 11. Likewise, “about 10 to about 20” contemplates 9 to 22 and 11 to 18. In the absence of the term “about,” the exact number is intended. In other words, “10” means 10.

Claims

CLAIMS What is claimed is:
1. A microsphere formulation, comprising: polymer microspheres, each polymer microsphere comprising: naltrexone; and a biodegradable polymer comprising a poly(ortho ester) (“POE”), wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of between about 25 mih to about 55 mih (Dso), with the proviso that the biodegradable polymer does not include poly (D,L-lactide-co-glycolide).
2. The microsphere formulation of claim 1, wherein the naltrexone comprises naltrexone in free base form.
3. The microsphere formulation of claim 1 or 2, wherein the POE comprises a cy cl ohexanedimethanohtri ethylene glycol (CHDM:TEG) co-polymer.
4. The microsphere formulation of any of the preceding claims, wherein the POE comprises a cy cl ohexanedimethanohtri ethylene glycol (CHDM:TEG) co-polymer in a ratio of about 93: about 7.
5. The microsphere formulation of any of claims 1, 2, or 3, wherein the POE comprises a cyclohexanedimethanohtriethylene glycol (CHDM:TEG) co-polymer in a ratio of about 88 to about 12.
6. The microsphere formulation of claim 1 or 2, wherein the POE comprises a cyclohexanedimethanoftri ethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri-block polymer.
7. The microsphere formulation of any of claims 1, 2, or 6, wherein the POE comprises a cyclohexanedimethanoktriethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri-block polymer in a ratio of about 88: about 10: about 2.
8. The microsphere formulation of any of claims 1, 2, or 6, wherein the POE comprises a cyclohexanedimethanoktriethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri-block polymer in a ratio of about 70: about 0: about 30.
9. The microsphere formulation of claim 1 or 2, wherein the POE comprises a 3,9- diethylidene-2,4,8,10-tetraoxaspiro[5.5]undecane:triethylene glycol (DETOSU:TEG).
10. The microsphere formulation of claim 1 or 2, wherein the POE comprises a 3,9- diethylidene-2,4,8, 10-tetraoxaspiro[5.5]undecane:tri ethylene glycol :tri ethylene glycol glycolide (DETOSU:TEG:TEG-GL).
11. The microsphere formulation of any one of the preceding claims, wherein each polymer microsphere comprises a drug load of about 45% to about 55% by weight of the polymer microsphere.
12. The microsphere formulation of any one of the preceding claims, wherein each polymer microsphere comprises a drug load of about 50% by weight of the polymer microsphere.
13. The microsphere formulation of any one of the preceding claims, wherein the polymer microspheres have an average particle size of about 25 mih to about 45 mih (Dso).
14. A pharmaceutical composition comprising the microsphere formulation of any one of the preceding claims.
15. A microsphere formulation, comprising: polymer microspheres, each polymer microsphere comprising: naltrexone; and a biodegradable polymer comprising a cy cl ohexanedimethanohtri ethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri -block polymer in a ratio of about 70: about 0: about 30, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of between about 25 mih to about 55 mih (Dso), with the proviso that the biodegradable polymer does not include poly (D,L-lactide-co-glycolide).
16. A microsphere formulation, comprising: polymer microspheres, each polymer microsphere comprising: naltrexone; and a biodegradable polymer comprising a cy cl ohexanedimethanohtri ethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri -block polymer in a ratio of about 88: about 10: about 2, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of between about 25 mih to about 55 mih (Dso), with the proviso that the biodegradable polymer does not include poly (D,L-lactide-co-glycolide).
17. A method for making polymer microspheres comprising naltrexone, the method comprising:
(i) contacting naltrexone with a cyclohexanedimethanoktri ethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri-block polymer in the presence of an organic solvent system comprising dichloromethane and benzyl alcohol to form a dispersed phase;
(ii) combining the dispersed phase with a continuous phase comprising water and surfactant in a homogenizer to form an emulsion;
(iii) removing the organic solvent from the emulsion to form a microsphere formulation essentially free of organic solvent; and
(iv) subjecting the substantially organic solvent-free microsphere formulation to freeze- drying.
18. The method of claim 17, wherein the surfactant comprises polyvinyl alcohol.
19. The method of claim 17 or 18, wherein the surfactant comprises polyvinyl alcohol in a concentration in the continuous phase prior to the combining of about 0.35% by weight.
20. A polymer microsphere formulation made according to the method of any one of preceding claims 17, 18, or 19.
21. A kit, compri sing : polymer microspheres, each polymer microsphere comprising:
(i) naltrexone; and
(ii) a cyclohexanedimethanoktri ethylene glycol :tri ethylene glycol glycolide (CHDM:TEG:TEG-GL) tri-block polymer, wherein each polymer microsphere comprises a drug load of naltrexone of at least 40% by weight of the polymer microsphere, and wherein the polymer microspheres have an average particle size of from about 25 mih (D50) to about 55 mih (D50).
22. The kit of claim 21, wherein the co-polymer is present in a ratio of either about 88: about
10: about 2 or about 70: about 0: about 30.
EP22772358.2A 2021-03-15 2022-03-03 Microsphere formulations comprising naltrexone and methods for making and using the same Pending EP4308106A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US202163161159P 2021-03-15 2021-03-15
US202163161187P 2021-03-15 2021-03-15
US202263266660P 2022-01-11 2022-01-11
PCT/US2022/070941 WO2022198167A1 (en) 2021-03-15 2022-03-03 Microsphere formulations comprising naltrexone and methods for making and using the same

Publications (1)

Publication Number Publication Date
EP4308106A1 true EP4308106A1 (en) 2024-01-24

Family

ID=83321294

Family Applications (1)

Application Number Title Priority Date Filing Date
EP22772358.2A Pending EP4308106A1 (en) 2021-03-15 2022-03-03 Microsphere formulations comprising naltrexone and methods for making and using the same

Country Status (2)

Country Link
EP (1) EP4308106A1 (en)
WO (1) WO2022198167A1 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7425292B2 (en) * 2001-10-12 2008-09-16 Monosol Rx, Llc Thin film with non-self-aggregating uniform heterogeneity and drug delivery systems made therefrom
US20080293695A1 (en) * 2007-05-22 2008-11-27 David William Bristol Salts of physiologically active and psychoactive alkaloids and amines simultaneously exhibiting bioavailability and abuse resistance
JP6282231B2 (en) * 2012-01-23 2018-02-21 アラーガン、インコーポレイテッドAllergan,Incorporated Sustained release biodegradable or bioerodible microspheres or microparticles suspended in a solid depot-forming injectable drug formulation

Also Published As

Publication number Publication date
WO2022198167A1 (en) 2022-09-22

Similar Documents

Publication Publication Date Title
JP6678571B2 (en) High drug-containing buprenorphine microsphere and method for producing the same
CA2765695C (en) Method of making sustained release microparticles
US9636308B2 (en) High drug load buprenorphine microspheres and method of producing same
EP4308106A1 (en) Microsphere formulations comprising naltrexone and methods for making and using the same
WO2022226505A1 (en) Microsphere formulations comprising nalmefene and methods for making and using the same
US20240000772A1 (en) Microsphere formulations comprising naltrexone and methods for making and using the same
US20220054420A1 (en) Microsphere formulations comprising ketamine and methods for making and using the same
US11992559B2 (en) Microsphere formulations comprising lurasidone and methods for making and using the same
WO2023097204A1 (en) Microsphere formulations comprising asenapine and methods for making and using the same
CA3210001A1 (en) Microsphere formulations comprising btk inhibitors and methods for making and using the same
WO2024097696A1 (en) Mixed release profile polymer microsphere formulations comprising octreotide and methods for making and using the same
US20230404922A1 (en) Microsphere formulations comprising btk inhibitors and methods for making and using the same
CN116916920A (en) Microsphere formulations comprising lurasidone and methods of making and using the same
US20230225993A1 (en) Microsphere formulations comprising ketamine and methods for making and using the same
WO2023133554A2 (en) Microsphere formulations comprising ketamine and methods for making and using the same
WO2019079095A2 (en) Composition and method of preparation of risperidone extended release preparation
WO2022192838A1 (en) Methods and systems for making polymer microspheres
WO2022226534A2 (en) Microsphere formulations comprising multiple non-identical peptides and methods for making the same

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20230929

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR