FULVESTRANT FORMULATIONS AND METHODS OF THEIR USE

Abstract
The disclosure is directed to fulvestrant formulations including suspensions of fulvestrant particles suitable for injection. The formulations can comprise fulvestrant particles having an LD Dv(10) less than about 3 microns, for example, between about 1 micron to about 3 microns, an LD Dv(50) less than about 35 microns, for example, between about 2 microns and about 35 microns, and an LD Dv(90) less than about 120 microns, for example, between about 4 microns and about 120 microns. The formulations can comprise fulvestrant particles having a CE Dv(90) less than about 200 microns, for example, between about 10 microns and about 200 microns, a CE Dv(50) less than about 60 microns, for example, between about 5 microns and about 60 microns, and a CE Dv(10) less than about 25 microns, for example, between about 1 microns and about 25 microns.
Description
FIELD

The disclosure is directed to fulvestrant-containing formulations and methods of their use in the treatment of disease.


BACKGROUND

Fulvestrant, or 7-(9-(4,4,5,5,5-pentafluoropentylsulfinyl)nonyl)estra-1,3,5(10)-triene-3,17-diol, has the structure of formula (1):




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Fulvestrant is a selective estrogen receptor degrader (SERD) indicated for the treatment of hormone receptor positive metastatic breast cancer in postmenopausal women with disease progression following anti-estrogen therapy.


As with other steroidal-like compounds, fulvestrant has physical properties which make preparing fulvestrant pharmaceutical compositions difficult. Fulvestrant is a particularly lipophilic molecule, even when compared with other steroidal compounds, and its aqueous solubility is extremely low.


Due to the poor solubility and oral bioavailability of fulvestrant, the drug is currently administered via intramuscular injection of an oil-based fulvestrant formulation. The current commercial formulation of fulvestrant, FASLODEX™, is dosed at 500 mg and requires that two 5 mL injections of a 50 mg/mL fulvestrant formulation be administered intramuscularly. Each 5 mL injection contains 10% w/v alcohol, 10% w/v benzyl alcohol, and 15% w/v benzyl benzoate as co-solvents and made up to 100% w/v with castor oil as a further co-solvent and release rate modifier. Administration of the formulation is slow (1-2 minutes per injection) and painful, due to the viscous oil-based vehicle used to solubilize fulvestrant. A warning has been added to the FASLODEX™ label concerning painful injections, sciatica, neuropathic pain, and peripheral neuropathy.


It has been previously reported (U.S. Pat. No. 6,774,122 to AstraZeneca) that intra-muscular injections of fulvestrant in the form of an aqueous suspension were not suitable for use. Those suspensions resulted in extensive local tissue irritation at the injection site as well as a poor release profile due to the presence of fulvestrant in the form of solid particles. Furthermore, the fulvestrant release rate was reported as not clinically significant.


There is a need for fulvestrant formulations with improved dosing properties. The disclosure is directed to these and other important needs.


SUMMARY

The present disclosure provides formulations comprising fulvestrant particles. The disclosure also provides fulvestrant suspensions, preferably those having a fulvestrant concentration of equal to or greater than about 50 mg/mL. The disclosure also provides formulations comprising fulvestrant particles and a non-oil vehicle. Some aspects of the disclosure are directed to pharmaceutical compositions comprising fulvestrant particles having an LD Dv(90) greater than or equal to about 7 microns. Further aspects of the disclosure are directed to pharmaceutical compositions comprising fulvestrant particles having a CE Dv(90) less than about 200 microns, for example, between about 10 microns and about 200 microns, a CE Dv(50) less than about 60 microns, for example, between about 5 microns and about 60 microns, and a CE Dv(10) less than 25 microns, for example, between about 1 microns and about 25 microns. Other aspects of the disclosure are directed to pharmaceutical compositions comprising fulvestrant at a concentration of about 100 mg/mL, whereupon administration to a subject, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of the pharmaceutical compositions of the disclosure is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of a reference listed fulvestrant product. Other aspects of the disclosure are directed to fulvestrant formulations having a concentration of about 100 mg/mL and particular pharmacokinetic profiles. In other aspects, the disclosure is directed to pharmaceutical compositions comprising fulvestrant particles, wherein the fulvestrant concentration is about 40 to 125 mg/mL.


Methods of making and using the products described herein are also described.





BRIEF DESCRIPTION OF THE DRAWINGS

The summary, as well as the following detailed description, is further understood when read in conjunction with the appended drawings. For the purpose of illustrating the disclosure, there are shown in the drawings exemplary embodiments of the disclosure; however, the disclosure is not limited to the specific methods, compositions, and devices disclosed. In the drawings:



FIG. 1A depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines;



FIG. 1B depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines;



FIG. 2A depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines;



FIG. 2B depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines;



FIG. 2C depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines;



FIG. 3 depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines;



FIG. 4 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 5 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 6 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 7 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 8 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 9 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 10 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 11 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 12 depicts aspects of exemplary methods of preparation for fulvestrant suspensions of the present disclosure;



FIG. 13 depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines;



FIG. 14 depicts pharmacokinetic data for administration of commercial fulvestrant formulations (FASLODEX™) and some exemplary fulvestrant formulations of the present disclosure to canines; and



FIG. 15 depicts schematic representations of aspects of methods of preparation of some exemplary fulvestrant formulations of the present disclosure.





All callouts and annotations in the Figures are hereby incorporated into this description as if fully set forth herein.


DETAILED DESCRIPTION OF ILLUSTRATIVE EMBODIMENTS

The present disclosure may be understood more readily by reference to the following detailed description taken in connection with the accompanying figures and examples, which form a part of this disclosure. It is to be understood that this disclosure is not limited to the specific devices, methods, applications, conditions or parameters described and/or shown herein, and that the terminology used herein is for the purpose of describing particular embodiments by way of example only and is not intended to be limiting of the claimed disclosure.


As used in the specification including the appended claims, the singular forms “a,” “an,” and “the” include the plural, and reference to a particular numerical value includes at least that particular value, unless the context clearly dictates otherwise.


When a range of values is expressed, another embodiment includes from the one particular value and/or to the other particular value. All ranges are inclusive and combinable. Further, reference to values stated in ranges include each and every value within that range. When values are expressed as approximations, by use of the antecedent “about,” it will be understood that the particular value forms another embodiment. The term “about” as used herein when referring to a measurable value such as an amount, a temporal duration, and the like, is meant to encompass reasonable variations of the value, such as, for example, ±10% from the specified value. For example, the phrase “about 50%” can include ±10% of 50, or from 45% to 55%.


It is to be appreciated that certain features of the disclosure which are, for clarity, described herein in the context of separate embodiments, may also be provided in combination in a single embodiment. Conversely, various features of the disclosure that are, for brevity, described in the context of a single embodiment, may also be provided separately or in any subcombination.


Terms

As used herein, whether by itself or in conjunction with another term or terms, it should be understood that the phrases “method of treating” and “method of treatment” may be used interchangeably with the phrase “for use in the treatment of” a particular disease.


As used herein, whether by itself or in conjunction with another term or terms, “pharmaceutically acceptable” indicates that the designated entity such as, for example, e.g., a pharmaceutically acceptable excipient is generally chemically and/or physically compatible with other ingredients in a formulation, and/or is generally physiologically compatible with the recipient thereof.


As used herein, “pharmaceutical composition” refers to a formulation as described herein that includes one or more pharmaceutically acceptable excipients, that is suitable for administration to a subject. It should be understood that the term “pharmaceutical composition” encompasses (a) suspensions and (b) suspensions which have been dried such that one or more solvents have been removed partially or completely, either by evaporation or sublimation, including, but not limited to, lyophilized cakes.


As used herein, whether by themselves or in conjunction with another term or terms, “subject(s),” “individual(s),” and “patient(s)”, refer to mammals, including humans. The term human(s) refers to and includes, a human child, adolescent, or adult.


As used herein, whether by themselves or in conjunction with another term or terms, “treats,” “treating,” “treated,” and “treatment,” refer to and include ameliorative, palliative, and/or curative uses and results, or any combination thereof. In other embodiments, the methods described herein can be used prophylactically. It should be understood that “prophylaxis” or a prophylactic use or result do not refer to nor require absolute or total prevention (i.e., a 100% preventative or protective use or result). As used herein, prophylaxis or a prophylactic use or result refer to uses and results in which administration of a compound or formulation diminishes or reduces the severity of a particular condition, symptom, disorder, or disease described herein; diminishes or reduces the likelihood of experiencing a particular condition, symptom, disorder, or disease described herein; or delays the onset or relapse (reoccurrence) of a particular condition, symptom, disorder, or disease described herein; or any combination of the foregoing.


As used herein, whether used alone or in conjunction with another term or terms, “therapeutic” and “therapeutically effective amount”, refer to an amount of a compound or formulation that (a) treats a particular condition, symptom, disorder, or disease described herein; (b) attenuates, ameliorates or eliminates one or more symptoms of a particular condition, disorder, or disease described herein; (c) delays the onset or relapse (reoccurrence) of a particular condition, symptom, disorder, or disease described herein. It should be understood that the terms “therapeutic” and “therapeutically effective” encompass any one of the aforementioned effects (a)-(c), either alone or in combination with any of the others (a)-(c).


As used herein, whether used alone or in conjunction with another term or terms, “therapeutic agent” refers to any substance included in a formulation that is useful in the treatment of a disease, condition, or disorder or comorbidity (i.e., a disease, condition, or disorder that exists simultaneously with breast cancer) and is not fulvestrant.


As used herein, whether used alone or in conjunction with another term or terms, “suspension” refers to solid particles dispersed in a liquid vehicle.


As used herein, whether used alone or in conjunction with another term or terms, “formulation” refers to a mixture of components. The term “formulation” encompasses pharmaceutical compositions, and suspensions, as well as suspensions that have been dried such that one or more solvents have been removed partially or completely (e.g., lyophilized cakes).


As used herein “Dv(10)”, “Dv(50)” and “Dv(90)” are defined as the volume weighted particle diameters where a cumulative 10%, 50% or 90% v/v of the particles have an equal or smaller diameter, respectively, when measured. For example, if a particle population has a Dv(50) of about 25 microns, 50% of the particles in volume have a diameter of less than or equal to about 25 microns.


As used herein, Dn(10)”, “Dn(50)” and “Dn(90)” are defined as the number weighted particle diameters where a cumulative 10%, 50% or 90% of the particles have an equal or smaller diameter, respectively, when measured. For example, if a particle population has a Dn(50) of about 25 microns, 50% of the particles in number have a diameter of less than or equal to about 25 microns.


Particle size and particle size distributions can be determined by measurement via laser diffraction. Particle size analysis by laser diffraction methods is known in the art and is explained more fully by ISO 13320:2009(E), “Particle size analysis—Laser diffraction methods,” International Organization for Standardization which is incorporated by reference herein in its entirety for all purposes. Particle sizes determined by laser diffraction are represented as the diameter of a sphere having equivalent volume to the particle volume as determined by Mie theory of light scattering. Tables 1-7 and 23-27 and FIGS. 4-12 provide laser diffraction particle size and particle size distribution (“PSD”) data for some exemplary embodiments of the present invention, with measurements taken during methods of preparation, on the day of formulation (“Day 0”), and at various later dates after formulation, as indicated. Measurements were taken “as is” and “sonicated.” Data for “sonicated” samples indicates that the measurement sample was subjected to sonication to disperse agglomerates and provide stable repeat measurements, as more fully described in ISO 13320:2009(E). Values measured via laser diffraction are indicated as such in the Figures and Tables, or are referred to herein by “laser diffraction Dv(##)”, “LD Dv(##)”, “laser diffraction diameter”, or “LD diameter.”


Particle size and particle size distributions can also be determined by microscopy image capture and analysis. Microscopy image capture and analysis captures a two dimensional (2D) image of a 3D particle and calculates various size and shape parameters from the 2D image. Particle sizes determined by microscopy image capture and analysis are represented as the diameter of a circle with the equivalent area as the 2D image of the particle, referred to herein as a circle equivalent or “CE” diameter. Particle size analysis by microscopy image capture and analysis is known in the art and is explained more fully by ISO 13322-1:2014, “Particle size analysis—Image analysis methods—Part 1: Static image analysis methods,” International Organization for Standardization, which is incorporated by reference herein in its entirety for all purposes. Values measured by microscopy image capture and analysis are referred to herein by “circle equivalent diameter,” “CE diameter,” “circle equivalent Dv(##),” “CE Dv(##)”, or “CE Dn(##)”. Tables 41-50 provide microscopy image capture and analysis particle size and particle size distribution data for some exemplary embodiments of the present invention, with measurement samples taken during methods of preparation, after an initial suspension is formed, or after lyophilization and reconstitution, as indicated.


A. Formulations
Suspensions Comprising Fulvestrant Particles and a Vehicle

In particular embodiments, the invention is directed to suspensions comprising fulvestrant particles and a vehicle. The fulvestrant particles may have different particle size distributions as described more fully elsewhere herein. As used herein, a “vehicle” is a suspending medium, preferably a pharmaceutically acceptable suspending medium. In certain embodiments, the vehicle is a non-oil vehicle. As used herein, “oils” are non-polar substances that have no or low miscibility with water. Castor oil is an example of an oil. In other embodiments of the invention, the vehicle comprises water, i.e., is aqueous. As used herein, an “aqueous” vehicle is a vehicle that comprises at least about 50% w/w water. In some embodiments, the aqueous vehicle comprises at least about 60% w/w, at least about 70% w/w, at least about 80% w/w, at least about 85% w/w, at least about 90% w/w, at least about 95% w/w, at least about 96% w/w, at least about 97% w/w, at least about 98% w/w, or at least about 99% w/w water. In certain embodiments of the invention, the vehicle is water. In yet other embodiments of the invention, the vehicle is a non-aqueous medium. In some embodiments, a vehicle comprises a single suspending medium. In other embodiments, a vehicle comprises a mixture of two or more suspending mediums, which may be aqueous or non-aqueous. In still other embodiments of the invention, the vehicle comprises both water and a non-aqueous solvent. In particular embodiments of the invention, the suspension is substantially oil-free. As used herein, a “substantially oil-free” suspension is a suspension comprising a vehicle that comprises at most about 10% w/w oil. In some preferred embodiments, a substantially oil-free suspension comprises a vehicle that comprises less than about 5% w/w oil, less than about 2% w/w oil, less than about 1% w/w oil, less than about 0.5% w/w oil, less than about 0.1% w/w oil, or comprises a vehicle that is free of oil.


Fulvestrant suspensions of the disclosure can have fulvestrant present at a concentration of about 40 mg/mL to about 125 mg/mL in a vehicle. The fulvestrant present in the fulvestrant suspensions may have different particle size distributions as described more fully elsewhere herein. In particular embodiments of the invention, fulvestrant is present at a concentration equal to or greater than about 40 mg/mL. In further embodiments, fulvestrant is present at a concentration of about 40 to about 75 mg/mL. In other embodiments, fulvestrant is present at a concentration of about 75 mg/mL to about 125 mg/mL. In still further embodiments, fulvestrant is present at a concentration of about 40 mg/mL, about 45 mg/mL, about 50 mg/mL, about 55 mg/mL, about 60 mg/mL, about 65 mg/mL, about 70 mg/mL, or about 75 mg/mL.


In certain embodiments, fulvestrant is present in the suspension at a concentration equal to or greater than about 75 mg/mL. In further embodiments, fulvestrant is present in the suspension at a concentration of about 75 to about 125 mg/mL. In particular embodiments, fulvestrant is present in the suspension at a concentration of about 80 mg/mL, about 85 mg/mL, about 90 mg/mL, about 95 mg/mL, about 100 mg/mL, about 105 mg/mL, about 110 mg/mL, about 115 mg/mL, about 120 mg/mL, or about 125 mg/mL. In other embodiments, fulvestrant is present in the suspension at a concentration of about 75 mg/mL to about 95 mg/mL, about 80 mg/mL to about 100 mg/mL, about 90 mg/mL to about 110 mg/ml, about 95 mg/mL to about 105 mg/mL, about 95 mg/mL to about 115 mg/mL, about 100 mg/mL to about 110 mg/mL, about 110 mg/mL to about 125 mg/mL, including all ranges and subranges there between.


Pharmaceutical Compositions Comprising Fulvestrant

Other embodiments of the disclosure include pharmaceutical compositions comprising fulvestrant. These pharmaceutical compositions may be prepared by combining fulvestrant, as described herein, with one or more additional excipients, preferably pharmaceutically acceptable excipients.


In certain embodiments, the pharmaceutical compositions may further comprise a stabilizer, or one or more stabilizers, or two or more stabilizers. In still further embodiments of the invention, the stabilizer is selected from the group consisting of surfactants, polymers, cross-linked polymers, buffering agents, electrolytes, and non-electrolytes. In yet further embodiments of the invention, the pharmaceutical composition comprises a combination of two or more stabilizers selected from the group consisting of surfactants, polymers, cross-linked polymers, buffering agents, electrolytes, and non-electrolytes.


In certain embodiments of the invention, the pharmaceutical compositions comprising fulvestrant comprise about 0.2 mg/mL to about 75 mg/mL of one or more stabilizers, and all ranges and subranges therebetween. In particular embodiments of the invention, the pharmaceutical composition comprises about 0.2 to 0.7 mg/mL, 0.5 to 1 mg/mL, 1 to 5 mg/mL, 2 to 8 mg/mL, 5 to 6 mg/mL, 5 to 10 mg/mL, 8 to 12 mg/mL, 10 to 15 mg/mL, 15 to 20 mg/mL, 20 to 30 mg/mL, 30 to 40 mg/mL, 40 to 50 mg/mL, 45 to 55 mg/mL, 50 to 60 mg/mL, or 60 to 75 mg/mL of one or more stabilizers, and all ranges and subranges there between. In further embodiments of the invention, the pharmaceutical composition comprises about 0.2 mg/mL, 0.5 mg/mL, 1 mg/mL, 2 mg/mL, 3 mg/mL, 4 mg/mL, 5 mg/mL, 5.5 mg/mL, 6 mg/mL, 7 mg/mL, 8 mg/mL, 9 mg/mL, 10 mg/mL, 12 mg/mL, 15 mg/mL, 17 mg/mL, 20 mg/mL, 25 mg/mL, 30 mg/mL, 35 mg/mL, 40 mg/mL, 45 mg/mL, 50 mg/mL, 55 mg/mL, 60 mg/mL, 65 mg/mL, 70 mg/mL, or about 75 mg/mL of one or more stabilizers.


In yet further embodiments of the invention, the stabilizer is a surfactant. For example, the stabilizer can be, but is not limited to, polyethylene oxide (PEO), a PEO derivative, polysorbate 80, polysorbate 20, poloxamer 188 (including, but not limited to, PLURONIC® F-68 poloxamer sold by BASF Corp. (Wyandotte, Mich., USA)), poloxamer 124 (including, but not limited to, PLURONIC® L44 poloxamer sold by BASF Corp. (Wyandotte, Mich., USA)), poloxamer 407 (including, but not limited to, PLURONIC® F127 poloxamer sold by BASF Corp. (Wyandotte, Mich., USA)), polyethoxylated vegetable oils, polyethoxylated castor oil (including but not limited to KOLLIPHOR® EL, formerly known as CREMOPHOR® EL sold by BASF Corp. (Wyandotte, Mich., USA)), sorbitan palmitate (including, but not limited to, SPAN™ 40 sold by Croda International Plc), lecithin, poly(vinyl alcohol) (“PVA”), human serum albumin, and mixtures thereof.


In particular embodiments of the invention, the stabilizer is a polymer. For example, the stabilizer can be, but is not limited to, a polyvinylpyrrolidone (“PVP”) (such as, but not limited to povidone K12, povidone K17, including as sold under the tradenames PLASDONE™ C-12 povidone, PLASDONE™ C-17 povidone, and PLASDONE™ C-30 povidone, and mixtures thereof), polyethylene glycol 3350, and mixtures thereof.


In other embodiments of the invention, the stabilizer is an electrolyte, i.e., a salt that dissociates into anions and cations in aqueous solution. For example, the stabilizer can be, but is not limited to, sodium chloride, calcium chloride, and mixtures thereof.


In still other embodiments of the invention, the stabilizer is a non-electrolyte, i.e., is non-ionic. For example, the stabilizer can be, but is not limited to, dextrose, glycerol (also referred to as glycerin), mannitol, or mixtures thereof.


In other embodiments of the invention, the stabilizer is a cross-linked polymer. For example, the stabilizer can be, but is not limited to, carboxymethylcellulose sodium (CMC). In some embodiments of the invention, the carboxymethylcellulose sodium stabilizer is CMC 7LF, CMC 7MF, CMC 7HF, or mixtures thereof.


In other embodiments of the invention, the stabilizer is a buffering agent, for example, NaH2PO4.H2O, NaH2PO4.2H2O, anhydrous NaH2PO4, sodium citrate, citric acid, Tris, sodium hydroxide, HCl, or mixtures thereof.


In further embodiments of the invention, combinations of non-electrolyte stabilizers and electrolyte stabilizers may be used. In some embodiments, the combination of stabilizers may comprise two or more non-electrolyte stabilizers. In other embodiments, the combination of stabilizers may comprise two or more electrolyte stabilizers. In further embodiments, the combination of stabilizers may comprise one or more non-electrolyte stabilizers and one or more electrolyte stabilizers. In yet further embodiments, the combination of stabilizers may comprise two or more of mannitol, dextrose, and sodium chloride.


In certain embodiments of the invention, combinations of surfactant stabilizers and polymer stabilizers may be used. In some embodiments, the combination of stabilizers may comprise two or more surfactant stabilizers. In other embodiments, the combination of stabilizers may comprise two or more polymer stabilizers. In further embodiments, the combination of stabilizers may comprise one or more surfactant stabilizers and one or more polymer stabilizers. In yet further embodiments, the combination of stabilizers may comprise two or more of polysorbate 80, polysorbate 20, and poloxamer 188. In still further embodiments, the combination of stabilizers may comprise one or more of polysorbate 80, polysorbate 20, and poloxamer 188 and one or more of povidone K12, povidone K17, polyvinylpyrrolidone as sold under the tradenames PLASDONE™ C-12 povidone, PLASDONE™ C-17 povidone, or PLASDONE™ C-30 povidone, and polyethylene glycol 3350. In yet still further embodiments, the combination of stabilizers may comprise polysorbate 80 and one or more of polyvinylpyrrolidone as sold under the tradename PLASDONE™ C-12 povidone and povidone K12.


In certain embodiments, the pharmaceutical compositions comprising fulvestrant comprise CMC (carboxymethylcellulose sodium). In some embodiments, the CMC is prepared and heat sterilized before being combined with the fulvestrant during methods of preparation (described more fully elsewhere herein). In further embodiments of the invention, the viscosity of a CMC solution can be modulated by the degree of heating applied, which can allow for the formation of a plurality of fulvestrant pharmaceutical compositions having identical constituents, but with different viscosity values. These different viscosity values can affect the physical stability of the fulvestrant pharmaceutical compositions and the pharmacokinetic characteristics upon administration to subjects. In some embodiments, fulvestrant pharmaceutical compositions comprising CMC may be prepared in two or more parts with each part comprising a different amount of CMC. In other embodiments one or more such parts may be a suspension free of any CMC. In further embodiments, the parts can be mixed in an appropriate ratio to obtain a desired pharmaceutical composition.


In certain embodiments of the invention, the pharmaceutical compositions in the form of liquid suspensions comprising fulvestrant and one or more stabilizers may exhibit different sedimentation behaviors to form either flocculated or caked suspension upon storage. In some embodiments of the invention, after being stored, pharmaceutical compositions in the form of liquid suspensions comprising fulvestrant can be redispersed back into a homogeneous suspension with an acceptable particle size distribution upon redispersion. Exemplary liquid suspension formulations described herein were prepared and tested for sedimentation and redispersion. The tested formulations exhibited different sedimentation behaviors, but all were redispersible back to an acceptable, homogeneous suspension after a 3-month storage period at room temperature.


In certain embodiments of the invention, the pharmaceutical compositions comprising fulvestrant have a pH of from about 3-10, for example, about 3, 4, 5, 6, 7, 8, 9, or about 10. In further embodiments of the invention, the pharmaceutical composition has a pH of from about 5-8. In further embodiments of the invention, the pharmaceutical composition has a pH of from about 6-8. In further embodiments of the invention, the pharmaceutical composition has a pH of from about 3-7. In certain embodiments of the invention, the pharmaceutical composition has a pH of about 6.0 to 8.0. In particular embodiments of the invention, the pharmaceutical composition has a pH of about 6.0 to 7.0, 6.5 to 7.0, 6.5 to 7.5, 6.7 to 7.2, 7.0 to 7.2, 7.0 to 7.5, or 7.0 to 8.0. In further embodiments of the invention, the pharmaceutical composition has a pH of about 7.0.


In particular embodiments of the invention, the pharmaceutical composition further comprises one or more buffering agents, i.e., an agent that when added to a pharmaceutical composition, results in a pharmaceutical composition that resists pH changes or that results in a change in pH, such as, but not limited to, NaH2PO4.H2O, NaH2PO4.2H2O, anhydrous NaH2PO4, sodium citrate, citric acid, Tris, sodium hydroxide, HCl, or mixtures thereof. In certain embodiments of the invention, the pharmaceutical composition comprises about 1 mM to 20 mM, of one or more buffering agents, and all ranges and subranges therebetween. In particular embodiments of the invention, the pharmaceutical composition comprises about 1 to 2 mM, 1 to 3 mM, 1 to 5 mM, 2 to 8 mM, 5 to 6 mM, 5 to 10 mM, 8 to 12 mM, 10 to 15 mM, or 15 to 20 mM of one or more buffering agents, and all ranges and subranges there between. In further embodiments of the invention, the pharmaceutical composition comprises about 1 mM, 2 mM, 3 mM, 4 mM, 5 mM, 6 mM, 7 mM, 8 mM, 9 mM, 10 mM, 11 mM, 12 mM, 13 mM, 14 mM, 15 mM, 16 mM, 17 mM, 18 mM, 19 mM, or 20 mM of one or more buffering agents.


In certain embodiments of the invention, the pharmaceutical composition has an osmolarity from about 280 mOsm/L to about 310 mOsm/L, for example, about 280, 285, 290, 300, 305, or about 310 mOsm/L. In further embodiments of the invention, the pharmaceutical composition has an osmolarity from about 290 mOsm/L to about 300 mOsm/L. In yet further embodiments of the invention, the pharmaceutical composition has an osmolarity of about 290 mOsm/L. In some embodiments, the osmolarity may be selected through the use of appropriate amounts of the one or more stabilizers, e.g., stabilizers that also act as tonicifiers, such as, but not limited to, the non-electrolyte stabilizers and electrolyte stabilizers described herein. In some embodiments, the osmolarity may be selected through the use of appropriate amounts of one or more buffering agents that act as tonicifiers in a pharmaceutical composition, such as, but not limited to, the buffering agents described herein.


In certain embodiments of the invention, the pharmaceutical composition has an absolute viscosity measured at 25° C. from about 1.0 cP to about 1000 cP, and all ranges and subranges therebetween. In particular embodiments of the invention, the pharmaceutical composition has an absolute viscosity measured at 25° C. from about 750 cP to about 1000 cP, about 500 to about 750 cP, about 250 cP to about 500 cP, about 100 cP to about 250 cP, about 50 cP to about 100 cP, about 25 cP to about 50 cP, about 10 cP to about 25 cP, about 1 cP to about 10 cP, about 1 cP to about 5 cP, about 1.0 cP to about 4.0 cP, about 1.0 cP to about 3.0 cP, about 1.0 cP to about 2.5 cP, about 1.0 cP to about 2.0 cP, about 1.5 cP to about 2.0 cP. In further embodiments of the invention, the pharmaceutical composition has an absolute viscosity measured at 25° C. of about 1.0 cP, 1.1 cP, 1.2 cP, 1.3 cP, 1.4 cP, 1.5 cP, 1.6 cP, 1.7 cP, 1.8 cP, 1.9 cP, 2.0 cP, 2.1 cP, 2.2 cP, 2.3 cP, 2.4 cP, 2.5 cP, 2.6 cP, 2.7 cP, 2.8 cP, 2.9 cP, 3.0 cP, 3.5 cP, 4.0 cP, 4.5 cP, 5.0 cP, 10 cP, 15 cP, or 20 cP.


In yet further embodiments of the invention, pharmaceutical compositions having a fulvestrant concentration of 50 mg/mL or 100 mg/mL have an absolute viscosity measured at 25° C. that is from about 2-fold to about 500-fold lower than FASLODEX™, and all ranges and subranges therebetween. In further embodiments of the invention, fulvestrant pharmaceutical compositions having a fulvestrant concentration of 50 mg/mL or 100 mg/mL have an absolute viscosity measured at 25° C. that is 500-fold lower, about 400-fold lower, about 300-fold lower, about 250-fold lower, about 200-fold lower, about 150-fold lower, about 100-fold lower, about 50-fold lower, about 40-fold lower, about 30-fold lower, about 20-fold lower, about 10-fold lower, about 5-fold lower, about 4-fold lower, about 3-fold lower, about 2-fold lower, or about 1.5-fold lower than FASLODEX™. In further embodiments of the invention, for example, fulvestrant pharmaceutical compositions having a fulvestrant concentration of 50 mg/mL or 100 mg/mL, have an absolute viscosity measured at 25° C. that is substantially equivalent to FASLODEX™. Table 21 provides density measurements of some exemplary fulvestrant pharmaceutical compositions of the present disclosure. Table 22 provides viscosity measurements of some exemplary fulvestrant pharmaceutical compositions of the present disclosure.


In certain embodiments of the invention, the pharmaceutical composition comprises one or more additional pharmaceutically acceptable excipients. As used herein, a pharmaceutically acceptable excipient is generally chemically and/or physically compatible with other ingredients in a pharmaceutical composition or pharmaceutical composition, and/or is generally physiologically compatible with the recipient thereof. In some embodiments, the one or more additional pharmaceutically acceptable excipients are selected from the group consisting of preservatives, antioxidants, or mixtures thereof. In yet further embodiments of the invention, the additional pharmaceutically acceptable excipient is a preservative such as, but not limited to, phenol, cresol, p-hydroxybenzoic ester, chlorobutanol, or mixtures thereof. In yet further embodiments of the invention, the additional pharmaceutically acceptable excipient is an antioxidant such as, but not limited to, ascorbic acid, sodium pyrosulfite, palmitic acid, butylated hydroxyanisole, butylated hydroxytoluene, tocopherols, or mixtures thereof.


In certain embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5.8 mg/mL of one or more stabilizers, and water for injection (WFI) q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of one or more surfactants, about 0.8 mg/mL of one or more polymers, and WFI q.s. to volume.


In yet further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 0.8 mg/mL of povidone K12 (PVP 12K), and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5.8 mg/mL of one or more stabilizers, about 9 mg/mL of one or more electrolytes, about 10 mM of one or more buffering agents, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of one or more surfactants, about 0.8 mg/mL of one or more polymers, about 9 mg/mL of sodium chloride, about 10 mM of one or more of NaH2PO4.H2O, NaH2PO4.2H2O, and anhydrous NaH2PO4 (preferably a mixture of about 0.61 mg/mL NaH2PO4.2H2O and about 0.85 mg/mL of anhydrous NaH2PO4), and WFI q.s. to volume


In certain embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 55 mg/mL of one or more stabilizers, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of one or more surfactants, about 50 mg/mL of one or more non-electrolytes, and WFI q.s. to volume.


In yet further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 50 mg/mL of dextrose, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of one or more stabilizers, about 9 mg/mL of one or more electrolytes, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of one or more surfactants, about 9 mg/mL of sodium chloride, and WFI q.s. to volume.


In yet further embodiments of the invention, the pharmaceutical composition comprises about 50 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 9 mg/mL of sodium chloride, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 55 mg/mL of one or more stabilizers, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of one or more surfactants, about 50 mg/mL of one or more non-electrolytes, and WFI q.s. to volume.


In yet further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 56.6 mg/mL of one or more stabilizers, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of one or more surfactants, about 1.6 mg/mL of one or more polymers, about 50 mg/mL of one or more non-electrolytes, and WFI q.s. to volume.


In yet further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 1.6 mg/mL of polyvinylpyrrolidone as sold under the tradename PLASDONE™ C-12 povidone, povidone K12, or a mixture thereof, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 57.4 mg/mL of one or more stabilizers, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of one or more surfactants, about 2.4 mg/mL of one or more polymers, about 50 mg/mL of one or more non-electrolytes, and WFI q.s. to volume.


In yet further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 2.4 mg/mL of polyvinylpyrrolidone as sold under the tradename PLASDONE™ C-12 povidone, povidone K12, or a mixture thereof, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, between about 1 mg/mL and 2.4 mg/mL of PVP, sorbitan palmitate, poloxamer 188, poloxamer 124, poloxamer 427, polyethoxylated castor oil, PVA, or a mixture thereof, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 2.4 mg/mL of PVA, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In yet further embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 1.0 mg/mL of polyethoxylated castor oil, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 2.0 mg/mL of poloxamer 188, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 1.5 mg/mL of poloxamer 188, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 1.5 mg/mL of sorbitan palmitate, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 1.5 mg/mL of poloxamer 124, about 50 mg/mL of mannitol, and WFI q.s. to volume.


In certain embodiments of the invention, the pharmaceutical composition comprises about 100 mg/mL fulvestrant, about 5 mg/mL of polysorbate 80, about 1.5 mg/mL of poloxamer 407, about 50 mg/mL of mannitol, and WFI q.s. to volume.


Aspects of some exemplary embodiments of pharmaceutical compositions comprising fulvestrant are shown in Tables 1-20 and 23-27.


In the Figures and specification, references are made to exemplary formulations. Some exemplary formulations are identified as “F###” where each “#” is a numeral, e.g., F001, F002, and so on. The exemplary formulations sharing an initial identification “F###” share identical concentrations of constituent components (mg/mL), but may vary in their properties due to different methods of preparation, particle size distributions of fulvestrant, or other differences in processing, storage, or handling. Such exemplary formulation sharing an initial identification scheme “F###” are further identified by extra alphanumeric characters. For example, the exemplary formulations F003a, F003b, and F003k2 have the same concentrations of constituent components but may differ in, e.g., the underlying methods of preparation and resulting particle size distributions. In some instances in the Figures, formulations are identified by only ending non-zero numerals # or ## and subsequent alphanumeric characters; for example, formulation F003a may be referred to as “Variant 3a”, formulation F005a2 may be referred to as “Variant 5a2”, and the like. Some exemplary formulations are identified and referred to as “Lot”s, with references to the same Lot number referring to exemplary formulations having the same concentrations of constituent components, but may vary in their properties due to different methods of preparation, particle size distributions of fulvestrant, or other differences in processing, storage, or handling.












TABLE 1





Target Formulation





(mg/mL)
Formulation B
Formulation E
Formulation I


















Fulvestrant
50
50
50


Polysorbate 80
5
5
5


PVP 12K
0.8
0.8
0.8


NaCl


9


WFI
q.s. to volume
q.s. to volume
q.s. to volume


Assay (% LC)
100.0
93.5
94.0


Total Impurities (% a/a)
0.2
0.3
0.2













PSD
as is
sonicated
as is
sonicated
as is
sonicated


(via laser diffraction)




















Day 0
LD Dv (10)
7.4
6.0
2.4
1.9
NA
NA


(μm)
LD Dv (50)
35.0
32.0
5.2
3.9





LD Dv (90)
143
129
11.1
8.7













(μm)

day 5
day 1
day 4















LD Dv (10)
7.6
2.3
2.3
1.2
2.5
0.04



LD Dv (50)
31.9
5.7
5.0
1.8
5.6
0.8



LD Dv (90)
107
19.2
10.9
2.5
12.3
3.2











(μm)

day 14
Day 10
Day 11















LD Dv (10)
5.9
5.1
1.9
1.8
2.3
0.06



LD Dv (50)
27.5
24.4
4.0
3.8
4.8
1.3



LD Dv (90)
86.3
76.0
9.1
9.4
9.4
3.7











(μm)

Day 77
Day 71
Day 12















LD Dv (10)
5.4
4.8
2.1
1.8
2.4
0.2



LD Dv (50)
26.3
21.0
4.7
3.8
5.1
3.0



LD Dv (90)
88.7
62.2
12.5
9.7
11.4
6.3










pH
7.4 (day 11)
6.9 (day 7)
7.1 (day 4) 


pH
N/A
N/A
6.9 (day 11)



















TABLE 2





Target Formulation





(mg/mL)
Formulation J
Formulation K
Formulation L


















Fulvestrant
50
50
100


Polysorbate 80
5
5
5


PVP 12K
0.8
0.8
0.8


NaCl
9
9
9


Phosphate buffer*
10 mM
10 mM
10 mM


WFI
q.s. to volume
q.s. to volume
q.s. to volume


Assay (% LC)
80.9
82.4
94.1


Total Impurities (% a/a)
0.2
0.2
0.2













PSD
as is
sonicated
as is
sonicated
as is
sonicated


(via laser diffraction)




















Day 0
LD Dv (10)
2.2
1.8
0.04
0.04
2.4
1.9


(μm)
LD Dv (50)
5.4
4.2
1.9
1.1
5.0
4.1



LD Dv (90)
11.8
10.3
4.7
3.6
10.4
8.4











(μm)

day 5
day 4
Day 0















LD Dv (10)
2.0
1.7
0.03
0.04
2.4
1.9



LD Dv (50)
4.7
3.8
1.4
1.1
5.0
4.1



LD Dv (90)
9.7
8.2
3.6
3.0
10.4
8.4











(μm)

Day 12
Day 11
Day 11















LD Dv (10)
2.1
1.8
1.8
0.05
2.0
2.0



LD Dv (50)
5.2
4.2
3.6
2.1
4.0
4.0



LD Dv (90)
14.8
14.5
6.9
4.9
7.6
7.8











(μm)

Day 13
Day 12
Day 11















LD Dv (10)
2.3
1.9
2.2
0.06
2.5
2.2



LD Dv (50)
5.9
4.6
4.5
2.3
5.3
5.0



LD Dv (90)
16.5
16.0
11.1
5.6
10.8
10.6










pH

7.0 (day 4) 
7.0 (day 1) 


pH

7.0 (day 11)
7.1 (day 12)


















TABLE 3





Target Formulation (mg/mL)
Formulation L3F
Formulation L6

















Fulvestrant
50
100


Polysorbate 80
5
5


PVP 12K
0.8
0.8


NaCl
9
9


Phosphate buffer*
10 mM
10 mM


WFI
q.s. to volume
q.s. to volume


Assay (mg/mL)
83.8
113.9


Total Impurities (% a/a)
0.7
0.2














PSD






(via laser diffraction)
as is
sonicated
as is
sonicated















Day 0 (μm)
LD Dv(10)
2.1
2.0
2.2
2.1



LD Dv(50)
5.9
5.5
6.9
6.7



LD Dv(90)
14.7
14.2
17.6
17.7













(μm)

Day 14
Day 1
















LD Dv(10)
2.1
2.0
2.1
2.1



LD Dv(50)
5.7
5.5
6.8
6.6



LD Dv(90)
14.4
14.0
18.0
17.7









pH

7.1 (day 1)



















TABLE 4





Target Formulation
F003a
F003b
F004a


















Fulvestrant
100
100
100


Polysorbate 80
5
5
5


Dextrose
50
50



NaCl


9


WFI
q.s. to volume
q.s. to volume
q.s. to volume


Manufacturing Process
API size reduction
API size reduction
API size reduction



by HSM only
by HSM followed
by HSM followed




by HPH
by HPH


Assay (mg/mL)
95.0
96.3
99.8


Total Impurities (%
0.42
0.28
0.27













PSD
as is
sonicated
as is
sonicated
as is
sonicated


(via laser diffraction)




















Day 0
LD
1.9
1.9
2.2
1.6
1.9
1.5


(μm)
LD
5.3
5.2
6.0
3.9
5.8
3.5



LD
13.0
12.7
12.1
7.6
12.2
7.7











(μm)

Day 13
Day 13
Day 13















LD Dv (10)
1.9
1.9
2.1
1.7
1.7
1.5



LD Dv (50)
5.3
5.2
5.5
4.2
4.0
3.3



LD Dv (90)
13.4
13.0
11.3
8.2
8.7
6.8











(μm)

Day 13
Day 13
Day 13















LD Dv (10)
1.8
1.7
2.1
1.7
1.7
1.6



LD Dv (50)
5.1
4.9
5.9
4.3
4.0
3.4



LD Dv (90)
13.0
13.2
12.1
8.4
8.6
6.3










pH

7.3 (Day 0) 
7.5 (Day 0) 


pH

7.1 (Day 13)
7.1 (Day 13)



















TABLE 5





Target Formulation





(mg/mL)
F003e
F003k2
F003k3


















Fulvestrant
100
100
100


Polysorbate 80
5
5
5


Dextrose
50
50
50


WFI
q.s. to volume
q.s. to volume
q.s. to volume


Manufacturing Process
Micronized API
Micronized API
Micronized API



dispersed by vortex/
dispersed by HSM
dispersed by HSM



sonics or HSM

followed by HPH





for size reduction


Assay (mg/mL)
100.5
97.8
99.6


Total Impurities (% a/a)
0.34
0.43
0.42













PSD
as is
sonicated
as is
sonicated
as is
sonicated


(via laser diffraction)




















Day 0
LD Dv (10)
1.5
1.5
1.5
1.4
2.2
1.4


(μm)
LD Dv (50)
3.9
3.8
2.9
2.6
7.0
3.4



LD Dv (90)
13.0
12.8
6.7
6.3
13.3
7.4











(μm)

Day 1
Day 5
Day 1















LD Dv (10)
1.5
1.5
NA
NA
NA
NA



LD Dv (50)
4.0
4.0







LD Dv (90)
12.4
12.5















(μm)

Day 13
Day 12
Day 8















LD Dv (10)
1.5
1.5
1.6
1.5
1.5
1.3



LD Dv (50)
4.1
4.1
3.2
2.9
2.9
2.6



LD Dv (90)
14.0
14.3
7.0
6.5
5.7
5.2











(μm)

Day 22
Day 12
Day 8















LD Dv (10)
1.5
1.5
1.5
1.4
1.4
1.1



LD Dv (50)
3.9
3.9
3.0
2.8
2.8
1.9



LD Dv (90)
12.6
12.8
6.7
6.4
6.2
3.5












pH

7.2
(day 1)
7.2
(day 0)


pH

4.5
(Day 12)
6.8
(Day 8)






















TABLE 6







Target Formulation
















(mg/mL)
F003i
F005a2
F005b1













Fulvestrant
100
100
100


Polysorbate 80
5
5
5


Dextrose
50




Mannitol

50
50


WFI
q.s. to volume
q.s. to volume
q.s. to volume


Manufacturing Process
Reconstituted
Reconstituted
Micronized API













lyophilized suspension,
lyophilized
dispersed by HSM




micronized API
suspension, API sized





dispersed by HSM
reduction by HSM











Assay (mg/mL)
99.2
93.2
100.2


Total Impurities (% a/a)
0.46
0.55
0.36
















PSD








(via laser diffraction)
as is
sonicated
as is
sonicated
as is
sonicated

















Day 0 (μm)
LD
4.6
1.7
2.1
2.0
1.5
1.4



LD
54.2
5.6
6.5
5.6
3.2
2.7



LD
112
16.2
18.4
13.5
7.9
6.6














(μm)

Day 9
Day 8
Day 13


















LD
2.5
1.5
2.1
2.0





LD
39.5
4.3
6.2
5.4





LD
95.1
13.5
16.7
13.2





Day(90)



















pH



6.5
(Day3)
7.4 (Day 0)














pH



7.2
(Day 9)





















TABLE 7





Target Formulation





(mg/mL)
F005c2
F0017a
F0015a


















Fulvestrant
100
100
100


Polysorbate 80
5
15
25


Mannitol
50
50
50


WFI
q.s. to volume
q.s. to volume
q.s. to volume


Manufacturing Process
Micronized API
Micronized API
Micronized API



dispersed by HSM
dispersed by HSM
dispersed by HSM



followed by HPH





for size reduction




Assay (mg/mL)
100.2

103.8


Total Impurities (% a/a)


0.39













PSD
as is
sonicated
as is
sonicated
as is
sonicated


(via laser diffraction)




















Day 0
LD
1.3
1.1
1.5
1.4
1.5
1.4


(μm)
LD
2.3
1.9
3.0
2.6
2.9
2.6



LD
4.9
3.7
7.2
6.4
6.9
6.4










pH

7.1 (day 0)
7.1 (day 0)

















TABLE 8








Formulation/Variants














mg/mL
I
J
K
L
M
N
O, O2

















Fulvestrant
50
50
50
100
100
100
100


Polysorbate 80
5
5
5
5
5
5
5


Povidone K12
0.8
0.8
0.8
0.8
0.8
0.8
0.8


Sodium
9
9
9
9
9
4.5



Chloride









Dextrose





25
50


NaH2PO4•2H2O

0.61
0.61
0.61





Na2HPO4

0.85
0.85
0.85





WFI
QS
QS
QS
QS
QS
QS
QS

















TABLE 9








Formulation




















F005








F003

F005a, a2,








F003a, b,

b1, c, c2,
F015

F017


variants
F001
F002
e, f, g, h, i,
F004
c3, d, d1, g,
F015a,

F017a,


(mg/mL)
F001e
B, E
j, k2, k3, l
F004a
g4, g5, h3
a1, a3
F016
a1, a3


















Fulvestrant
100
100
100
100
100
100
100
100


Polysorbate 80
5
5
5
5
5
25
5
15


Povidone K12

0.8




0.8



Sodium



9






Chloride










Dextrose


50







Mannitol




50
50
50
50


WFI
QS
QS
QS
QS
QS
QS
QS
QS

















TABLE 10








Formulation

















(mg/mL)
F003k+
F006
F007
F008
F009
F010
F011
F012
F013
F014




















Fulvestrant
200
100
100
100
100
100
100
100
100
100


Polysorbate 80
5
25
5
5
5
5
5
5
5
5


Dextrose
50
50
50
50
50
50
50
50
50
50


Polysorbate 20


15









Poloxamer 188



2








PVP K12




20







PVP K17





5






PEG 3350






60





CMC7LF PH







30




CMC7MF PH








20



CMC7HF PH









5


WFI
QS
QS
QS
QS
QS
QS
QS
QS
QS
QS



























TABLE 11





(mg/mL)
F018
F019
F020
F021
F022
F023
F024
F025
F026
F027
F028


























Fulvestrant
100
100
100
100
100
100
100
100
100
100
100


Polysorbate 80
5
5
5
5
5
5
5
5
5
5
5


Polysorbate 20




5
15

5
15
5



Poloxamer 188






2
2
2
2



Mannitol
50
50
50
50
50
50
50
50
50
50
50


Dextrose













NaCl













Glycerol













PVP K12
5
10
20






10



PVP K17



5









PEG 3350










60


CMC7LF PH













CMC7MF PH













CMC7HF PH













WFI
qs
qs
qs
qs
qs
qs
qs
qs
qs
qs
qs
























TABLE 12





(mg/mL)
F029
F030
F031
F032
F033
F034
F035
F036























Fulvestrant
100
100
100
100
100
100
100
100


Polysorbate 80
5
5
5
5
5
5
5
5


Polysorbate 20







5


Poloxamer 188







2


Mannitol
50
25
12.5
37.5
50
50
50
50


Dextrose

25
37.5
12.5






NaCl










Glycerol
30









PVP K12







5


PVP K17










PEG 3350










CMC7LF PH




3
2
1
1


CMC7MF PH










CMC7HF PH










WFI
qs
qs
qs
qs
qs
qs
qs
qs



























TABLE 13





(mg/mL)
F037
F038
F039
F040
F041
F042
F043
F044
F045
F046
F047


























Fulvestrant
100
100
100
100
100
100
100
100
100
100
100


Polysorbate 80
5
5
5
5
5
5
5
5
5
5
5


Polysorbate 20



5



5





Poloxamer 188



2



2





Mannitol
25
25
25
25
12.5
12.5
12.5
12.5
37.5
37.5
37.5


Dextrose
25
25
25
25
37.5
37.5
37.5
37.5
12.5
12.5
12.5


NaCl













Glycerol













PVP K12



5



5





PVP K17













PEG 3350













CMC7LF PH
3
2
1
1
3
2
1
1
3
2
1


CMC7MF PH













CMC7HF PH













WFI
qs
qs
qs
qs
qs
qs
qs
qs
qs
qs
qs
























TABLE 14





(mg/mL)
F048
F049
F050
F051
F052
F053
F054
F055























Fulvestrant*
100
100
100
100
100
100
100
100


Polysorbate 80
5
5
5
5
5
5
5
5


Polysorbate 20
5






5


Poloxamer 188
2






2


Mannitol
37.5
25
25
25
25
25
25
25


Dextrose
12.5


25
25
25
25
25


NaCl

4.9
9
4.9
4.9
4.9
4.9
4.9


Glycerol










PVP K12
5






5


PVP K17










PEG 3350










CMC7LF PH
1



3
2
1
1


CMC7MF PH










CMC7HF PH










WFI
qs
qs
qs
qs
qs
qs
qs
qs























TABLE 15





(mg/mL)
F056
F057
F058
F059
F060
F061
F062







Fulvestrant
100
100
100
100
100
100
100


Polysorbate 80









Polysorbate 20
 5
 10
 15
 5
 5
 10
 10


Poloxamer 188









Mannitol
 50
 50
 50
 50
 50
 50
 50


Dextrose









NaCl









Glycerol









PVP K12









PVP K17









PEG 3350



 10
 30
 10
 30


PEG 4000









CMC7LF PH









CMC7MF PH









CMC7HF PH









WFI
qs
qs
qs
qs
qs
qs
qs
























TABLE 16





(mg/mL)
F063
F064
F065
F066
F067
F068
F069
F070







Fulvestrant
100
100
100
100
100
100
100
100


Polysorbate 80










Polysorbate 20
 15
 15
 5
 5
 10
 10
 15
 15


Poloxamer 188










Mannitol
 50
 50
 50
 50
 50
 50
 50
 50


Dextrose










NaCl










Glycerol










PVP K12










PVP K17










PEG 3350
 10
 30








PEG 4000


 3
   7.5
 3
   7.5
 3
   7.5


CMC7LF PH










CMC7MF PH










CMC7HF PH










WFI
qs
qs
qs
qs
qs
qs
qs
qs

















TABLE 17








Formulations/Variants















Component
Q
R
S
T
U
V
W
X


















Fulyestrant (mg/mL)
100
100
100
100
100
100
100
100


Polysorbate 80
25
5


5
5

5


(mg/mL)










Polysorbate 20


5







(mg/mL)










Poloxamer 188



5






(mg/mL)










Lecithin (mg/mL)






5



PVP K12 (mg/mL)
0.8
5
0.8
0.8


0.8
0.8


PVP K17 (mg/mL)




0.8





PEG 3350 (mg/mL)





50












Dextrose (mg/mL)
50




Sodium Chloride

9
13















(mg/mL)










NaOH
QS to
QS to
QS to
QS to
QS to
QS to
QS to
QS to



pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0


HC1
QS to
QS to
QS to
QS to
QS to
QS to
QS to
QS to



pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0


WFI
QS to
QS to
QS to
QS to
QS to
QS to
QS to
QS to



volume
volume
volume
volume
volume
volume
volume
volume

















TABLE 18








Formulations/Variants















Component
1
2
3
4
5
6
7
8


















Fulvestrant
100
100
100
100
100
100
100
100


(mg/mL)










Polysorbate 80

5


5
5

5


(mg/mL)










Polysorbate 20


5







(mg/mL)










Poloxamer 188



5






(mg/mL)










Human Serum
5









Albumin (mg/mL)










Lecithin (mg/mL)






5



PVP K12
0.8
5
0.8
0.8


0.8
0.8


(mg/mL)










PVP K17




0.8





(mg/mL)










PEG 3350





50




(mg/mL)


















Dextrose
50
50
















(mg/mL)


















Mannitol (mg/mL)


50















Citric buffer
QS to
QS to
QS to
QS to
QS to
QS to
QS to
QS to



pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0
pH 7.0


WFI
QS to
QS to
QS to
QS to
QS to
QS to
QS to
QS to



volume
volume
volume
volume
volume
volume
volume
volume

























TABLE 19





Formulation
F005g4
Lot
Lot
Lot
Lot
Lot
Lot
Lot
Lot


(mg/mL)
F005g5
15
26
27
28
42
43
X1
X2
























Fulvestrant
100
100
100
100
100
100
100
100
100


Polysorbate 80
5
5
5
5
5
5
5
5
5


PVPC12



1.6
1.6






Span 40





1.5





Pluronic F-68






1.5




Pluronic L44







1.5



Pluronic F127








1.5


Mannitol (before
50
50

50

50
50
50
50


homogenization)











Mannitol (after


50

50






homogenization)































TABLE 20







Formulation
Lot
Lot
Lot
Lot



(mg/mL)
45
46
47
48






















Fulvestrant
100
100
100
100



Polysorbate 80
5
5
5
5



PVPC12
2.4






Span 40







Pluronic F-68

2





Cremophor EL


1




PVA



2.4



Mannitol
50
50
50
50



(before







homogenization)




















TABLE 21







Sample




Name
Density (g/ml)



















F003h
1.032



F003f
1.032



F003e
1.032



F003k2
1.030





















TABLE 22







Sample

Viscosity



Name
Formulation
(cps)









Placebo
5 mg/mL PS80 + 50 mg/mL
1.1




Dextrose




F003h
[Described elsewhere]
1.8



F003f
[Described elsewhere]
1.9



F003k
[Described elsewhere]
2.0



F003e
[Described elsewhere]
1.5










B. Fulvestrant Particles

Particular embodiments of the disclosure comprise solid fulvestrant particles, for example a fulvestrant suspension comprising solid fulvestrant particles. In certain embodiments of the invention, at least about 90% of the total fulvestrant in the formulation is present as solid particles. In further embodiments of the invention, at least about 80% of the total fulvestrant in the formulation is present as solid particles.


In certain embodiments of the invention, solid fulvestrant particles are particles consisting of crystalline and/or amorphous fulvestrant. In other embodiments of the invention, fulvestrant particles comprise crystalline and/or amorphous fulvestrant as well as other excipients. In still other embodiments, fulvestrant particles comprise crystalline and/or amorphous fulvestrant coated or surface modified by a surface modifier adsorbed on the surface of the particle. The surface modifier can be a stabilizer such as, but not limited to surfactants, polymers, electrolytes, and non-electrolytes, and mixtures thereof.


Other embodiments of the present invention may further comprise fulvestrant in forms other than a solid particle, such as, but not limited to, solubilized fulvestrant as a free molecule or associated with a suspension such as micelles, microemulsions, emulsion, liposome, and combinations thereof, or complexed with other formulation constituents in a vehicle. In further embodiments of the invention, such other forms of fulvestrant are in equilibrium with the fulvestrant solid particles.


In particular embodiments of the invention, the fulvestrant particles comprise about 90-99.9% by weight of fulvestrant and 0.1-10% by weight of a surface modifier adsorbed on the surface of said particle. In particular embodiments of the invention, the surface modifier is a stabilizer such as, but not limited to surfactants, polymers, electrolytes, and non-electrolytes, and mixtures thereof. In certain embodiments of the invention, fulvestrant particles comprise at least about 90% fulvestrant. In other embodiments of the invention fulvestrant particles comprise at least about 92%, 95%, 97%, 98%, 99%, 99.5%, or 99.9% fulvestrant.


In further embodiments of the invention, one or more solvents, such as water, present in the pharmaceutical composition can be removed partially or completely by appropriate techniques known to the art, such as lyophilization or spray drying, to form a dried pharmaceutical composition for reconstitution. In certain embodiments of the invention, the dried pharmaceutical composition can comprise up to about 1%, about 2%, about 5%, or about 10% of the one or more solvents. The dried pharmaceutical composition can be reconstituted with appropriate diluent known to the art, such as, but not limited to water for injection (WFI), normal saline (NS), and 5% dextrose in water (D5W) prior to administration. In further embodiments of the invention, the diluent can further comprise an organic solvent or one or more of the excipients described herein. Dried pharmaceutical compositions formed by lyophilization may be in the form of a lyophilized cake.


Fulvestrant Particle Sizes

In certain embodiments of the invention, the fulvestrant particles have a laser diffraction diameter greater than or equal to about 1 micron. In yet further embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 1 micron. In other embodiments of the invention the fulvestrant particles have a laser diffraction diameter greater than or equal to about 2 microns. In still other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 2 microns.


In certain embodiments of the invention, the fulvestrant particles have a laser diffraction diameter greater than or equal to about 0.5 microns. In other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 0.5 microns. In other embodiments of the invention, the fulvestrant particles have a laser diffraction diameter greater than or equal to about 1 micron. In other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 1 microns. In still other embodiments of the invention, the fulvestrant particles have a laser diffraction diameter greater than or equal to about 1.5 microns. In other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 1.5 microns. In yet other embodiments of the invention, the fulvestrant particles have a laser diffraction diameter greater than or equal to about 2 microns. In other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 2 microns.


In further embodiments of the invention, about 98% of fulvestrant particles have a laser diffraction diameter greater than or equal to about 0.5 microns. In other embodiments of the invention, about 98% of fulvestrant particles have a laser diffraction diameter greater than or equal to about 1 micron. In still other embodiments of the invention, about 98% of fulvestrant particles have a laser diffraction diameter greater than or equal to about 1.5 microns. In yet other embodiments of the invention, about 98% of fulvestrant particles have a laser diffraction diameter greater than or equal to about 2 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) between about 4 microns and about 120 microns, between about 4 microns and about 100 microns, between about 4 microns and about 75 microns, between about 4 microns and about 60 microns, between about 4 microns and about 50 microns, between about 4 microns and about 40 microns, between about 4 microns and about 30 microns, between about 4 microns and about 20 microns, between about 4 microns and about 15 microns, between about 4 microns and about 10 microns, between about 20 microns and about 60 microns, between about 20 microns and about 45 microns, between about 20 microns and about 30 microns, between about 30 microns and about 50 microns, or between about 4 microns and about 9 microns. In other embodiments of the invention, the fulvestrant particles have a LD Dv(90) equal to about 4 microns, about 5 microns, about 6 microns, about 7 microns, about 8 microns, about 9 microns, about 10 microns, about 11 microns, about 12 microns, about 13 microns, about 14 microns, about 15 microns, about 16 microns, about 17 microns, about 18 microns, about 19 microns, about 20 microns, about 25 microns, about 30 microns, about 35 microns, about 40 microns, about 45 microns, about 50 microns, about 55 microns, about 60 microns, about 65 microns, about 70 microns, about 75 microns, about 80 microns, about 85 microns, about 90 microns, about 95 microns, about 100 microns, about 105 microns, about 110 microns, about 115 microns, or about 120 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 120 microns. In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 100 microns. In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 80 microns. In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 60 microns. In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 50 microns. In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 40 microns. In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 30 microns. In further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 25 microns. In further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 18 microns. In further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 16 microns. In further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 14 microns. In still further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 11 microns. In yet further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 9 microns. In yet further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 7 microns. In yet further embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 5 microns. In particular embodiments of the invention, particles have an LD Dv(90) between about 9-14 microns. In other embodiments of the invention, the particles have an LD Dv(90) between about 12-14 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 9-11 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 7-9 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 6-8 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 6-7 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 3-6 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(50) between about 2 microns and about 35 microns, between about 2 microns and about 25 microns, between about 2 microns and about 20 microns, between about 2 microns and about 15 microns, between about 2 microns and about 10 microns, between about 2 microns and about 8 microns, between about 2 microns and about 7 microns, between about 2 microns and about 6 microns, between about 2 microns and about 5 microns, between about 2 microns and about 4 microns, between about 5 microns and about 10 microns, between about 5 microns and about 15 microns, between about 7 microns and about 10 microns, between about 8 microns and about 10 microns, or between about 9 microns and about 16 microns. In other embodiments of the invention, the fulvestrant particles have a LD Dv(50) equal to about 2 microns, 3 microns, 4 microns, about 5 microns, about 6 microns, about 7 microns, about 8 microns, about 9 microns, about 10 microns, about 11 microns, about 12 microns, about 13 microns, about 14 microns, about 15 microns, about 16 microns, about 17 microns, about 18 microns, about 19 microns, about 20 microns, about 25 microns, about 30 microns, or about 35 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(50) less than or equal to about 9 microns. In other embodiments of the invention, the particles have an LD Dv(50) less than or equal to about 7 microns. In other embodiments of the invention, the particles have an LD Dv(50) less than or equal to about 6 microns. In yet other embodiments of the invention, the particles have an LD Dv(50) less than or equal to about 5 microns. In particular embodiments of the invention, the particles have an LD Dv(50) less than or equal to about 4 microns. In further embodiments of the invention, the particles have an LD Dv(50) less than or equal to about 3 microns. In further embodiments of the invention, the particles have an LD Dv(50) between about 4-6 microns. In further embodiments of the invention, the particles have an LD Dv(50) between about 3-5 microns. In yet further embodiments of the invention, the particles have an LD Dv(50) between about 3-4 microns. In yet further embodiments of the invention, the particles have an LD Dv(50) between about 2-3 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(10) no more than about 3 microns, about 2 microns, or about 1 microns. In further embodiments of the invention, the particles have an LD Dv(10) between about 1 micron and about 3 microns. In still further embodiments of the invention, the particles have an LD Dv(10) greater than or equal to about 2 microns. In yet further embodiments of the invention, the particles have an LD Dv(10) between about 1.5 microns to about 2.5 microns. In yet further embodiments of the invention, the particles have an LD Dv(10) between about 1 micron to about 2 microns. In yet further embodiments of the invention, the particles have an LD Dv(10) between about 1.0 micron to about 1.5 microns. In even further embodiments of the invention, the particles have an LD Dv(10) of about 2 microns. In even further embodiments of the invention, the particles have an LD Dv(10) of about 1.5 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) less than or equal to about 25 microns and an LD Dv(50) less than or equal to about 9 microns. In particular embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 16 microns and an LD Dv(50) less than or equal to about 6 microns. In other embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 11 microns and an LD Dv(50) less than or equal to about 5 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 9 microns and an LD Dv(50) less than or equal to about 4 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) less than or equal to about 8 microns and an LD Dv(50) less than or equal to about 4 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) between about 9-14 microns and an LD Dv(50) between about 4-6 microns. In still other embodiments of the invention, the particles have an LD Dv(90) between about 9-11 microns and an LD Dv(50) between about 4-6 microns. In particular embodiments of the invention, the particles have an LD Dv(90) between about 12-14 microns and an LD Dv(50) between about 4-6 microns. In further embodiments of the invention, the particles have an LD Dv(90) between about 6-8 microns and an LD Dv(50) between about 2-4 microns. In further embodiments of the invention the fulvestrant particles have a laser diffraction diameter greater than or equal to about 1 micron. In yet further embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 1 micron. In other embodiments of the invention the fulvestrant particles have a laser diffraction diameter greater than or equal to about 2 microns. In still other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 2 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) between about 9-14 microns, an LD Dv(50) between about 4-6 microns, and an LD Dv(10) between about 2-3 microns. In other embodiments of the invention, the particles have an LD Dv(90) between about 9-11 microns, an LD Dv(50) between about 4-6 microns, and an LD Dv(10) between about 2-3 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 12-14 microns, an LD Dv(50) between about 4-6 microns, and an LD Dv(10) between about 2-3 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 6-9 microns, an LD Dv(50) between about 2-4 microns, and an LD Dv(10) between about 1-2 microns. In further embodiments of the invention the fulvestrant particles have a laser diffraction diameter greater than or equal to about 1 micron. In yet further embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 1 micron. In other embodiments of the invention the fulvestrant particles have a laser diffraction diameter greater than or equal to about 2 microns. In still other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 2 microns.


In certain embodiments of the invention, the fulvestrant particles have an LD Dv(90) between about 9-14 microns, an LD Dv(50) between about 4-6 microns, and an LD Dv(10) between about 2-3 microns, and the fulvestrant particles have a laser diffraction diameter greater than or equal to about 1 micron. In other embodiments of the invention, the particles have an LD Dv(90) between about 9-14 microns, an LD Dv(50) between about 4-6 microns, and an LD Dv(10) between about 2-3 microns, and at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 1 micron. In yet other embodiments of the invention, the fulvestrant particles have an LD Dv(90) between about 30 microns and about 110 microns, an LD Dv(50) between about 5 microns and about 30 microns, and an LD Dv(10) between about 1.5 microns and about 3 microns. In other embodiments of the invention, the particles have an LD Dv(90) between about 9-14 microns, an LD Dv(50) between about 4-6 microns, and an LD Dv(10) between about 2-3 microns, and the fulvestrant particles have a laser diffraction diameter greater than or equal to about 2 microns. In still other embodiments of the invention, the particles have an LD Dv(90) between about 9-14 microns, an LD Dv(50) between about 4-6 microns, and an LD Dv(10) between about 2-3 microns, and at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 2 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 6-9 microns, an LD Dv(50) between about 2-4 microns, an LD Dv(10) between about 1-2 microns, and the fulvestrant particles have a laser diffraction diameter greater than or equal to about 0.5 microns. In yet other embodiments of the invention, the particles have an LD Dv(90) between about 6-9 microns, an LD Dv(50) between about 2-4 microns, an LD Dv(10) between about 1-2 microns, and at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 0.5 microns. In further embodiments of the invention the fulvestrant particles have a laser diffraction diameter greater than or equal to about 1 micron. In yet further embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 1 micron. In other embodiments of the invention the fulvestrant particles have a laser diffraction diameter greater than or equal to about 2 microns. In still other embodiments of the invention, at least a portion of the fulvestrant particles have a laser diffraction diameter less than about 2 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dv(10) between about 1 microns and about 25 microns, between about 2 microns and about 25 microns, between about 3 microns and about 7 microns, between about 4 microns and about 15 microns, between about 4 microns and about 10 microns, between about 4 microns and about 8 microns, between about 6 microns and about 8 microns, between about 6 microns and about 7 microns, or between about 1 microns and about 10 microns. In other embodiments of the invention, the fulvestrant particles have a CE Dv(10) equal to about 1 micron, about 2 microns, about 3 microns, about 4 microns, about 5 microns, about 6 microns, about 7 microns, about 8 microns, about 9 microns, about 10 microns, about 11 microns, about 12 microns, about 13 microns, about 14 microns, about 15 microns, about 16 microns, about 17 microns, about 18 microns, about 19 microns, about 20 microns, about 21 microns, about 22 microns, about 23 microns, about 24 microns, or about 25 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dv(50) between about 5 microns and about 60 microns, between about 5 microns and about 50 microns, between about 9 microns and about 20 microns, between about 9 microns and about 15 microns, between about 10 microns and about 50 microns, between about 10 microns and about 40 microns, between about 10 microns and about 30 microns, between about 10 microns and about 20 microns, between about 15 microns and about 30 microns, between about 15 microns and about 25 microns, between about 15 microns and about 20 microns, or between about 10 microns and about 15 microns. In other embodiments of the invention, the fulvestrant particles have a CE Dv(50) equal to about 5 micron, about 6 microns, about 7 microns, about 8 microns, about 9 microns, about 10 microns, about 11 microns, about 12 microns, about 13 microns, about 14 microns, about 15 microns, about 16 microns, about 17 microns, about 18 microns, about 19 microns, about 20 microns, about 21 microns, about 22 microns, about 23 microns, about 24 microns, about 25 microns, about 30 microns, about 35 microns, about 40 microns, about 45 microns, about 50 microns, about 55 microns, or about 60 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dv(90) between about 10 microns and about 200 microns, between about 25 microns and about 150 microns, between about 25 microns and about 125 microns, between about 25 microns and about 100 microns, between about 25 microns and about 75 microns, between about 25 microns and about 50 microns, between about 25 microns and about 40 microns, between about 25 microns and about 35 microns, between about 35 microns and about 90 microns, between about 35 microns and about 75 microns, between about 35 microns and about 50 microns, between about 35 microns and about 45 microns, between about 50 microns and about 100 microns, between about 50 microns and about 75 microns, or between about 20 microns and about 40 microns. In other embodiments of the invention, the fulvestrant particles have a CE Dv(90) equal to about 10 microns, about 15 microns, about 20 microns, about 25 microns, about 30 microns, about 35 microns, about 40 microns, about 45 microns, about 50 microns, about 55 microns, about 60 microns, about 65 microns, about 70 microns, about 75 microns, about 80 microns, about 85 microns, about 90 microns, about 95 microns, about 100 microns, about 105 microns, about 110 microns, about 115 microns, about 120 microns, about 125 microns, about 130 microns, about 135 microns, about 140 microns, about 145 microns, about 150 microns, about 155 microns, about 160 microns, about 165 microns, about 170 microns, about 175 microns, or about 200 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dv(90) between about 35 microns and about 90 microns, a CE Dv(50) between about 10 microns and about 35 microns, and a CE Dv(10) between about 4 microns and about 10 microns. In other embodiments of the invention, the particles have a CE Dv(90) between about 25 microns and about 60 microns, a CE Dv(50) between about 10 microns and about 25 microns, and a CE Dv(10) between about 4 microns and about 8 microns. In other embodiments of the invention, the particles have a CE Dv(90) between about 20 microns and about 35 microns, a CE Dv(50) between about 10 microns and about 20 microns, and a CE Dv(10) between about 4 microns and about 8 microns. In still other embodiments of the invention, the particles have a CE Dv(90) between about 30 microns and about 100 microns, a CE Dv(50) between about 10 microns and about 50 microns, and a CE Dv(10) between about 4 microns and about 10 microns. In yet other embodiments of the invention, the particles have a CE Dv(90) between about 50 microns and about 100 microns, a CE Dv(50) between about 20 microns and about 50 microns, a CE Dv(10) between about 6 microns and about 8 microns. In yet other embodiments of the invention, the particles have a CE Dv(90) between about 50 microns and about 75 microns, a CE Dv(50) between about 30 microns and about 40 microns, a CE Dv(10) between about 8 microns and about 10 microns. In yet other embodiments of the invention, the particles have a CE Dv(90) between about 20 microns and about 60 microns, a CE Dv(50) between about 9 microns and about 20 microns, and a CE Dv(10) between about 3 microns and about 7 microns. In still further embodiments of the invention, the particles have a CE Dv(90) between about 20 microns and about 50 microns, a CE Dv(50) between about 9 microns and about 20 microns, and a CE Dv(10) between about 3 microns and about 7 microns. In other embodiments of the invention, the particles have a CE Dv(90) between about 20 microns and about 45 microns, a CE Dv(50) between about 9 microns and about 20 microns, and a CE Dv(10) between about 3 microns and about 7 microns. In yet further embodiments of the invention, the particles have a CE Dv(90) between about 20 microns and about 40 microns, a CE Dv(50) between about 9 microns and about 15 microns, and a CE Dv(10) between about 3 microns and about 7 microns. In further embodiments of the invention, the particles have a CE Dv(90) between about 20 microns and about 35 microns, a CE Dv(50) between about 9 microns and about 15 microns, and a CE Dv(10) between about 3 microns and about 7 microns. In still other embodiments of the invention, the particles have a CE Dv(90) between about 20 microns and about 45 microns, a CE Dv(50) between about 9 microns and about 15 microns, and a CE Dv(10) between about 3 microns and about 7 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dn(90) between about 4 microns and about 20 microns, between about 6 microns and about 15 microns, between about 6 microns and about 12 microns, between about 8 microns and about 12 microns, between about 8 microns and about 11 microns, between about 4 microns and about 10 microns, between about 4 microns and about 8 microns, between about 4 microns and about 7 microns, or between about 4 microns and about 6 microns. In other embodiments of the invention, the fulvestrant particles have a CE Dn(90) equal to about 4 microns, about 5 microns, about 6 microns, about 7 microns, about 8 microns, about 9 microns, about 10 microns, about 11 microns, about 12 microns, about 13 microns, about 14 microns, about 15 microns, about 16 microns, about 17 microns, about 18 microns, about 19 microns, or about 20 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dn(50) between about 2.0 microns and about 10.0 microns, between about 2.0 microns and about 8.0 microns, between about 2.0 microns and about 6.0 microns, between about 2.0 microns and about 5.0 microns, between about 3.0 microns and about 5.0 microns, between about 3.5 microns and about 4.5 microns, between about 2.0 microns and about 4.0 microns, between about 2.5 microns and about 4.5 microns, or between about 2.5 microns and about 3.5 microns. In other embodiments of the invention, the fulvestrant particles have a CE Dn(50) equal to about 2.0 microns, about 2.5 microns, about 3.0 microns, about 3.5 microns, about 4.0 microns, about 4.5 microns, about 5.0 microns, about 5.5 microns, about 6.0 microns, about 6.5 microns, about 7.0 microns, about 7.5 microns, about 8.0 microns, about 8.5 microns, about 9.0 microns, about 9.5 microns, or about 10.0 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dn(10) between about 0.5 microns and about 2.0 microns, between about 0.5 microns and about 1.5 microns, between about 1.0 microns and about 1.5 microns, between about 0.8 microns and about 1.2 microns, between about 0.9 microns and about 1.1 microns, or between about 0.5 microns and about 1.0 microns. In other embodiments of the invention, the fulvestrant particles have a CE Dn(10) equal to about 0.5, about 0.6, about 0.7, about 0.8, about 0.9, about 1.0, about 1.1, about 1.2, about 1.3, about 1.4, about 1.5, about 1.6, about 1.7, about 1.8, about 1.9, or about 2.0 microns.


In certain embodiments of the invention, the fulvestrant particles have a CE Dn(90) between about 4 microns and about 20 microns, a CE Dn(50) between about 2.0 microns and about 10.0 microns, and a CE Dn(10) between about 0.5 microns and about 2.0 microns. In other embodiments of the invention, the fulvestrant particles have a CE Dn(90) between about 6 microns and about 12 microns, a CE Dn(50) between about 2.0 microns and about 6.0 microns, and a CE Dn(10) between about 0.5 microns and about 1.5 microns. In further embodiments of the invention, the fulvestrant particles have a CE Dn(90) between about 8 microns and about 1 microns, a CE Dn(50) between about 3.0 microns and about 5.0 microns, and a CE Dn(10) between about 0.8 microns and about 1.2 microns.


C. Preparation Methods

In certain embodiments of the invention, formulations of the invention can be prepared from commercially available fulvestrant having different particle size distributions, such as, for example, recrystallized, micronized fulvestrant, or a combination thereof. In further embodiments of the invention, the formulations are prepared with sterilized, commercially available fulvestrant. In particular embodiments, commercially available fulvestrant is used in the formulations of the present invention without further processing for size reduction.


In other embodiments of the invention, fulvestrant particles suitable for use in formulations of the invention can be prepared from commercially available fulvestrant by any suitable methods known in the art. Suitable methods include, but are not limited to, size-reduction techniques such as milling, grinding, crushing, compression, attrition, low shear mixing, high shear mixing, high pressure homogenization, lyophilization, precipitation, or combinations thereof.


Desired particle size distributions for fulvestrant particles can be achieved by processing steps at one or more stages of formulation preparation. In some embodiments, the desired particle size distribution can be formed by processing fulvestrant material prior to suspension in media, by techniques described more fully elsewhere herein. In other embodiments, the desired particle size distribution can be formed by processing after suspension in media, by techniques described more fully elsewhere herein, including but not limited to high shear mixing and high pressure homogenization. In still other embodiments, the desired particle size distribution can be formed by a combination of the processing prior to and after suspension in media.


Suitable milling techniques include, but are not limited to, dry milling, wet milling, and cryogenic milling. Suitable milling machines include ball mills, pebble mills, rod mills, roller mills, colloid mills, impact mills, and jet mills. In certain embodiments of the invention, the particles can be reduced in size in the presence of one or more excipients or stabilizers, such as but not limited to a surfactants, polymers, electrolytes, and non-electrolytes, and mixtures thereof. Alternatively, the particles can be contacted with one or more excipients or stabilizers after they are reduced in size.


In certain embodiments of the invention, the formulations can be prepared from an un-milled commercially available fulvestrant by reducing the fulvestrant particle size with high shear mixing. In yet further embodiments of the invention, the formulations can be prepared from an un-milled, commercially available fulvestrant by reducing the fulvestrant particle size with high shear mixing followed by high pressure homogenization.


In certain embodiments of the invention, the formulations can be prepared from commercially available micronized fulvestrant by reducing the micronized fulvestrant particle size with high shear mixing (“HSM”). In yet further embodiments of the invention, the formulations can be prepared from an un-milled commercially available fulvestrant by reducing the fulvestrant particle size with high shear mixing followed by high pressure homogenization (“HPH”).


In some embodiments of the invention, the formulations can be prepared using high pressure homogenization. In further embodiments of the invention, the high pressure homogenization process reduces particle size by subjecting the particle population to one or more of cavitation, shear, and impact within a homogenization chamber under operating pressures from about 5,000 psi to about 45,000 psi, for example, about 5,000, 10,000, 15,000, 20,000, 25,000, 30,000, 35,000, 40,000 or about 45,000 psi. In yet further embodiments of the invention, the high pressure homogenization process is performed at about 40,000 psi. In some embodiments of the invention, the high pressure homogenization process is performed at operating pressures from about 15,000 psi to about 20,000 psi. In further embodiments, the formulations can be prepared by passing the formulation suspension through a homogenization chamber under operating pressures for one or more passes, for example, 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35, 36, 37, 38, 39, 40, 41, 42, 43, 44, 45, or 50 passes.


In the Figures and specification, references are made to exemplary formulations and processes for preparing exemplary formulations. Some exemplary preparation processes are identified with alphanumeric reference identifiers, such as “Process A1,” “Process A2,” and so on. Some exemplary formulations can share identical concentrations of constituent components (mg/mL), but may vary in their properties due to the different preparation processes, storage, or handling, which can result in different particle size distributions due to more or less size reduction, more or less aggregation or agglomeration, or both during processing, storage, or handling.


Methods of Forming Aqueous Fulvestrant Suspensions

In some embodiments of the invention, methods of forming an aqueous fulvestrant suspension comprise mixing an aqueous medium and at least one stabilizer to form a suspension vehicle, adding an amount of fulvestrant to the suspension vehicle, and dispersing the fulvestrant in the suspension vehicle to form the aqueous fulvestrant suspension. In further embodiments, these methods can further comprise homogenizing the aqueous fulvestrant suspension. In yet further embodiments, the methods with or without the homogenizing step can further comprise concentrating the fulvestrant suspension by phase separating the suspension and removing a portion of the supernatant. In particular further embodiments, after the concentrating step the methods can further comprise adding one or more electrolytes, non-electrolytes, buffering agents, or cross-linked polymers to the homogenized aqueous fulvestrant suspension and mixing the one or more electrolytes, non-electrolytes, buffering agents, or cross-linked polymers into the suspension. In some embodiments of the invention, the methods comprise a dispersing step performed using high shear mixing, a homogenizing step performed using high pressure homogenization, or both a dispersing step performed using high shear mixing and a homogenizing step performed using high pressure homogenization.


In further embodiments of the invention that include one or more stabilizers, the one or more stabilizers may be incorporated into the formulations at one or more stages of the methods of forming the formulations. In some embodiments, at least a portion or all of the stabilizers of a formulation are added to an aqueous medium along with an amount of fulvestrant prior to some or all of any mixing, homogenization, or supernatant-removal steps. In still other embodiments, at least a portion or all of the one or more stabilizers of a formulation are added to the fulvestrant suspensions after some or all of any mixing, homogenization, or supernatant-removal steps have been completed. In further embodiments, at least a portion or all of the surfactant and polymer stabilizers of the formulations are combined with the aqueous medium and fulvestrant prior to some or all of any mixing, homogenization, or supernatant-removal steps and at least a portion or all of the electrolyte, non-electrolyte, buffering agents, and cross-linked polymers of the formulations are added to the suspension after some or all of any mixing, homogenization, or supernatant-removal steps.


The fulvestrant particles described herein can be prepared in a method comprising the steps of dispersing fulvestrant particles in a liquid suspension medium and applying mechanical means in the presence of grinding media to reduce the particle size of fulvestrant to the desired size.


In further embodiments of the invention, a solvent, such as water, present in a formulation can be removed by appropriate techniques known to the art, such as lyophilization or spray drying, to form a dried formulation suitable for later reconstitution. Lyophilization can be used to produce a lyophilized (lyo) cake. The dried formulation can be reconstituted back into a liquid suspension using an appropriate diluent. Different volumes of diluent can be used to produce reconstituted suspensions with different fulvestrant concentrations as needed. The diluent can be aqueous in general but can further comprise an organic solvent and/or any excipient as described elsewhere herein.


In some embodiments of the invention, at least a portion of the formulation components other than fulvestrant can be omitted from the suspension and incorporated as part of the diluent and introduced into the suspension upon reconstitution by the diluent to arrive at the final formulation. In further embodiments, suspensions can be prepared with higher or lower concentrations of constituent components than desired in formulations for administration, formed into dried formulations and placed into vials in appropriate amounts of dried formulation to achieve target dose amounts of fulvestrant per vial for later reconstitution of diluent to form the desired formulation for administration.


Some exemplary methods of preparation of dried pharmaceutical compositions are depicted schematically in FIG. 15.


In some embodiments, the pharmaceutical compositions and dried pharmaceutical compositions can be prepared using aseptic process or terminally sterilized by a compatible sterilization technique, such as, but not limited to, gamma irradiation. When a polymer is used as an excipient in the pharmaceutical composition, said polymer such as carboxymethylcellulose (CMC) or its salts including sodium CMC, can be sterilized by autoclave in a solution then combined with rest of the pharmaceutical composition that is prepared aseptically or terminally sterilized.


Some aspects of exemplary embodiments of methods of preparation of the invention are shown in Tables 4-7 and 23-27 and FIGS. 4-12 and 15 which describe aspects of the preparation methods for exemplary fulvestrant formulations.















TABLE 23





Target








Formulation








(mg/mL)
B
E
I
J
K
L





















Fulvestrant
50
50
50
50
50
100


Polysorbate 80
5
5
5
5
5
5


PVP 12K
0.8
0.8
0.8
0.8
0.8
0.8


NaCl


9
9
9
9


Phosphate



10 mM
10 mM
10 mM


buffer








WFI
q.s. to
q.s. to
q.s. to
q.s, to
q.s. to volume
q.s. to volume


Starting API
Un-milled API
Un-milled API
Un-milled API
Un-milled API
Un-milled API
Un-milled API


(PSD via laser
L D Dv90: 780
L D Dv90: 780
L D Dv90: 780
L D Dv90: 1890
L D Dv90: 1890
L D Dv90: 1890


diffraction)
microns
microns
microns
microns
microns



Manufacturing
API size
API size
API size
API size
API size
API size


process
reduction
reduction
reduction
reduction
reduction
reduction



by HSM
by HSM
by HSM
by HSM
by HSM
by HSM




followed
followed
followed
followed
followed




by HPH
by HPH,
by HPH in
by HPH in
by HPH in





then
the presence
the presence
the presence





subsequent
of salts
of salts, then
of salts





salt

further HSM






addition





Process End
L D Dv90: 143
Total 15 min
Total 42 min
Total 45 min
Total 45 min
Total 25 min


Point Targets
HSM at
HSM at
HSM at
HSM at
HSM at
HSM at


(PSD via laser
micron
~20,000 rpm
~20,000 rpm
~25,000 rpm
~25,000 rpm
~25,000 rpm


diffraction)
HSM:
(L D Dv90:
(L D Dv90:
(L D Dv90:
(L D Dv90:
(L D Dv90:



Total 15
<~80 micron)
<~40 micron)
<~50 micron)
<~50 micron)
<~80 micron)



min at
HPH: 15
L D Dv90: 12.6
L D Dv90: 11.8
L D Dv90: 4.7
L D Dv90: 13.8



~20,000
passes in
micron
micron
micron
microns



rpm
reverse flow
HPH: 30
HPH: 3
HPH: 12
HPH: 15




through z5
passes in
passes in
passes in
passes in




nozzle at
parallel flow
parallel flow
parallel flow
parallel flow




~30,000 psi
through z5
through z5
through z5
through z8




L D Dv90:
nozzle at
nozzle at
nozzle at
nozzle at




11.1 micron
~40,000 psi
~40,000 psi
~40,000 psi to
~30,000 psi







L D Dv90: ~8








micron then








additional 5








min HSM at








~25,000 rpm






















TABLE 24





Target Formulation








(mg/mL)
L3F
L6
F003a
F003b
F004a
F003e





















Fulvestrant
100
100
100
100
100
100


Polysorbate 80
5
5
5
5
5
5


PVP 12K
0.8
0.8






NaCl
9
9






Phospate buffer
10 mM
10 mM


9



Dextrose


50
50

50


WFI
q.s. to
q.s. to
q.s. to
q.s. to
q.s. to
q.s. to


Starting API
Un-milled
Un-milled
Un-milled
Un-milled
Un-milled
Jet-milled


(PSD via
API
API
API
API
API
API


laser diffraction)

LD Dv90:
LD Dv90:
LD Dv90:
LD Dv90:






240 micron
240 micron
240 micron



Manufacturing
API size
API size
API size
API size
API size
API size


Process
reduction
reduction
reduction
reduction
reduction
dispersed



by HSM
by HSM
by HSM
by HSM
by HSM
by HSM





(F001e), then
followed by
followed by
and





subsequent
HPH, then
HPH, then
sonication/





dextrose
subsequent
subsequent
vortex





addition
dextrose
NaCl







addition
addition



Process End Point
LD Dv90:
LD Dv90:
LD Dv90:
Total 15 min
Total 15 min
LD Dv90:


Targets (PSD via
14.7 micron
17.6 micron
13.6 micron
HSM at
HSM at
12.2 micron


laser diffraction)
and
and
and
~25,000 rpm
~25,000 rpm
HSM: Total



LD Dv50:
LD Dv50:
LD Dv50:
to target
to target
5 min at



5.9 micron
6.9 micron
5.7 micron
LD Dv90:
LD Dv90:
~25,000 rpm



HSM: Total
HSM: Total
HSM: Total
<~40 micron
<~40 micron
to LD Dv90:



>120 min
>120 min
60-120 min at
LD Dv90:
LD Dv90:
12.6 micron



at ~25,000-
at ~25,000-
~25,000 rpm
15.1 micron
15.1 micron
by sonication/



30,000 rpm
30,000 rpm
before
HPH: 15 passes
HPH: 15 passes
vortex





dextrose
in parallel flow
in parallel flow






addition to
through z5
through z5






LD Dv90:
nozzle at
nozzle at






13.0 micron
~40,000 psi
~40,000 psi







before dextrose
before NaCl







addition to
addition to







LD Dv90:
LD Dv90:







12.1 micron
12.2 micron







pH = 7.3
pH = 7.5




















TABLE 25





Target






Formulation






(mg/mL)
F003k2
F003k3
F003l
F005a2



















Fulvestrant
100
100
100
100


Polysorbate 80
5
5
5
5


Dextrose
50
50
50



Mannitol



50


WFI
q.s. to
q.s. to
q.s. to volume
q.s. to volume


Starting API
Jet-mill API
Jet-mill API
Jet-mill API
Un-milled API


(PSD via laser
L D Dv90:
L D Dv90:
L D Dv90:
L D Dv90:


diffraction)
7-8 micron
7-8 micron
7-13 micron
240 micron


Manufacturing
API dispersed
API dispersed by
API dispersed by HSM
API size reduction by


process
by HSM, then
HSM then size
(F003i, f, j). Suspension
HSM (F001e), then



subsequent
reduction by HPH
lyophilized, reconstituted
mannitol addition.



dextrose
in the presence of
then composited
Suspension lyophilized,



addition
dextrose

reconstituted then






composited.


Process End
L D Dv90: 6.7
Total 5 min HSM
Total 5 min HSM at
L D Dv90: 1.3.6 micron


Point Targets
micron after
at
~25,000 rpm for
and L D Dv50:


(PSD via laser
dextrose
~25,000 rpm
dispersing each
5.7 micron


diffraction)
addition
(Dv90: 9.2
individual API lot
HSM: Total 60-120 min



HSM: Total 5
micron) for
F003i, f, j before
at



min at
dispersing API
lyophilization,
~25,000 rpm before



~25,000 rpm
L D Dv90: 13.3
L D Dv90:
mannitol addition to




micron HPH: 9
7.0, 12.9, 7.3 Micron
L D Dv90: 13.2 micron




passes in parallel
After reconstitution,
(F005a)




flow through z5
L D Dv90: 121,
After lyophilization,




nozzle at
113, 113 micron.
reconstitution,




~40,000 psi;
Composite F0031,
composite




dextrose co-
L D Dv90: 112 micron
F005a2, Dv90: 18.4




processed

micron






















TABLE 26





Target








Formulation








(mg/mL)
F005b1
F005c2
F0065c3
F005d1
F015a1
F015a3







Fulvestrant
100
100
100
100
100
100


Polysorbate 80
 5
 5
 5
 5
 25
 25


Mannitol
 50
 50
 50
 50
 50
 50


WFI
q.s. to
q.s. to
q.s. to
q.s. to
q.s. to
q.s. to


Starting API
Jet-mill API
Jet-mill API
Jet-mill API
Jet-mill API
Jet-mill API
Jet-mill API


(PSD via laser
L D Dv90:
L D Dv90:
L D Dv90:
L D Dv90:
L D Dv90:
L D Dv90:


diffraction)
7-8 micron
7-8 micron
7-8 micron
7-8 micron
7-8 micron
7-8 micron


Manufacturing
API
API
Lyophilized
API size
API
Lyophilized


process
dispersed
dispersed
F005c2
reduction
dispersed
F015a1



by HSM
by HSM

by HSM
by HSM




in the
then size

followed
in the




presence
reduction

by HPH,
presence




of mannitol
by HPH

then
of mannitol





in the

subsequent






presence of

mannitol






mannitol

addition




Process End
L D Dv90:
Total 5 min
After
Total 5 min
L D Dv90:
After


Point Targets
7.9
HSM at
reconstitution,
HSM at
6.9
reconstitution,


(PSD via laser
micron
~25,000
L D Dv90:
~25,000
micron
L D Dv90:


diffraction)
HSM:
rpm for
112
rpm for
HSM:
22.7



Total
dispersing
micron
dispersing
Total
micron



5 min at
API

API
5 min at




~25,000
(L D Dv90:

(L D Dv90:
~25,000




rpm
~7 micron)

~7 micron)
rpm





To HPH

To HPH






with 15

with 15






passes in

passes in






parallel

parallel






flow

flow






through z5

through z5






nozzle at

nozzle at






~40,000 psi

~40,000 psi






resulted in

resulted in






L D Dv90:

Dv90:






17.2 micron

~16 micron






pH = 7.1

(F001h4)








L D Dv90:








40 micron








after








mannitol








addition








pH = 7.1





















TABLE 27





Target







Formulation







(mg/mL)
F015a4
F017a1
F01733
F005g4
F005g5







Fulvestrant
100
100
100
100
100


Polysorbate 80
 25
 15
 15
 5
 5


Mannitol
 50
 50
 50
 50
 50


WFI
Qs. to
Qs. to
q.s. to
Qs. to
q.s. to


Starting API
Jet-mill API
Jet-mill API
Jet-mill API
Recrystallized API
Recrystallized API


(PSD via laser
L D Dv90: 7-8
L D Dv90: 7-8
L D Dv90: 7-8
L D Dv90: 18
L D Dv90: 18


diffraction)
micron
iiticron
micron
micron
micron


Manufacturing
F015a3 gamma
API dispersed
Lyophilized,
API dispersed
Lyophilized


process
irradiated at
by HSM in the
gamma
by HSM in the
F005g4



35 kGy
presence of
irradiated (35
presence of





mannitol
KGy) F017a1
mannitol



Process End
After
L D Dv90:
After
Total 5 min



Point Targets
reconstitution,
7.2
reconstitution,
HSM at



(PSD via laser
L D Dv90: 22.7
micron
L D Dv90: 31.9
~25,000 rpm for



diffraction)
micron
HSM:
micron
dispersing API





Total

(L D Dv90: ~20





5 min at

micron)





~25,000

L D Dv90: ~10





rpm

micron after HPH







with 9 passes in







parallel flow







through z5







nozzle at







~40,000 psi







Final







L D Dv90: 7.5







micron after







concentration









D. Pharmacokinetics

In certain embodiments of the invention, the pharmaceutical compositions are bioequivalent to the commercial pharmaceutical composition, FASLODEX™. The single dose PK parameters in postmenopausal advanced breast cancer patients administered FASLODEX™ dosed intramuscularly with 500 mg with an additional dose at day 15 are reported as, in geometric mean and coefficient of variation (%), Cmax 25.1 (35.3) ng/mL, Cmin 16.3 (25.9) ng/mL, and AUC 11,400 (33.4) ng·hr/mL.


In further embodiments of the invention, the 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) of the pharmaceutical composition of the invention is within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of FASLODEX™. In yet further embodiments of the invention, the 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) of the pharmaceutical composition of the invention is within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of FASLODEX™ in the fasting state. In still further embodiments of the invention, the 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) of the pharmaceutical composition of the invention is within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of FASLODEX™ in the fed state.


In other embodiments of the invention, the 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) of the pharmaceutical composition of the invention having a fulvestrant concentration of 100 mg/mL is within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of FASLODEX™. In still other embodiments of the invention, the 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) of the pharmaceutical composition of the invention having a fulvestrant concentration of 100 mg/mL is within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of FASLODEX™ in the fasting state. In yet other embodiments of the invention, the 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) of the pharmaceutical composition of the invention having a fulvestrant concentration of 100 mg/mL is within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of FASLODEX™ in the fed state.


In particular embodiments of the invention, the pharmaceutical composition has the single dose and multiple dose pharmacokinetic parameters shown in Tables 28 and 29. Table 28 shows pharmacokinetic parameters for 500 mg dosage of pharmaceutical compositions of the disclosure. For the data labeled “Single Dose” in Table 28, the fulvestrant blood plasma concentration data are shown for a 500 mg initial dose with an additional 500 mg dose given on day 15. For the data labeled “Multiple Dose Steady State” in Table 28, the fulvestrant blood plasma concentration data are shown for measurement at month 3, after a 500 mg dosage on days 1, 15, 20, and once monthly thereafter. Table 29 shows pharmacokinetic parameters for a single 250 mg dosage of pharmaceutical compositions of the disclosure. In Table 29, data are expressed as geometric mean (CV %), except for Tmax, which is shown as a median value with a range indicated in parentheses.












TABLE 28






Cmax (ng/mL)
Cmin (ng/mL)
AUC (ng · hr/mL)







Single Dose1
 20.08-31.375
13.04-20.375
 9,120-14,250


Multiple Dose
22.4-35.0
9.76-15.25
10,480-16,375


Steady State2























TABLE 29






I
II
III
IV
V
VI
VII







Cmax
 8.20
 4.76
8.2
  4-8.5
11.8 
8.3
 8-12


(μg/L)
(63.8) 
(68.1)


(6.6)
(8.8)



Cmin
 2.62
 2.38
2.6
2.0-3.0





(μg/L)
(33.4) 
(47.7)







Tmax
 6.97
8.8
7  
6-9
4.2
4.6
4-5


(days)
(1.86-7.95)
(6.97-12.0)


(8.3)
(11.2) 



AUC28
148  
88.4 
148   
 80-150
369  
333  
325-375


(μg · day/L)
(45.3) 
(47.3)


(4.1)
(3.0)









In particular embodiments, a dose of about 500 mg of a fulvestrant pharmaceutical composition of the invention is bioequivalent to 500 mg of the commercial pharmaceutical composition, FASLODEX™. In certain embodiments, a dose of less than 500 mg of a fulvestrant pharmaceutical composition of the invention is bioequivalent to 500 mg of the commercial pharmaceutical composition, FASLODEX™. In further embodiments, a dose of about 400 to 450 mg of a fulvestrant pharmaceutical composition of the invention is bioequivalent to 500 mg of the commercial pharmaceutical composition, FASLODEX™. In still further embodiments, a dose of about 350 to 400 mg of a fulvestrant pharmaceutical composition of the invention is bioequivalent to 500 mg of the commercial pharmaceutical composition, FASLODEX™. In yet further embodiments, a dose of about 300 to 350 mg of a fulvestrant pharmaceutical composition of the invention is bioequivalent to 500 mg of the commercial pharmaceutical composition, FASLODEX™. In even further embodiments, a dose of about 250 to 300 mg of a fulvestrant pharmaceutical composition of the invention is bioequivalent to 500 mg of the commercial pharmaceutical composition, FASLODEX™


In other embodiments of the invention, a 500 mg dose of a pharmaceutical composition of the invention provides 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of a 500 mg dose of FASLODEX™.


In other embodiments of the invention, a dose of less than 500 mg of a pharmaceutical composition of the invention provides 90% confidence intervals (CI) of the relative mean Cmax, AUC(0-t) and AUC(0-∞) within 80% to 125% of the relative mean Cmax, AUC(0-t) and AUC(0-∞), respectively, of a 500 mg dose of FASLODEX™


In some embodiments of the invention, fulvestrant pharmaceutical compositions of the invention can be administered as a single intramuscular injection, with the 90% confidence intervals (CI) of the relative mean Cmax, AUC(0−t) and AUC(0−∞) of fulvestrant is within 80% to 125% of the relative mean Cmax, AUC(0−t) and AUC(0−∞), respectively, of fulvestrant after administration of 500 mg of fulvestrant in the form of FASLODEX™ administered intramuscularly as two 5 mL injections. In further embodiments, such fulvestrant pharmaceutical compositions administered as a single intramuscular injection comprise a dose of about 500 mg of fulvestrant. In yet further embodiments, such fulvestrant pharmaceutical compositions administered as a single intramuscular injection comprise a dose of about 500 mg of fulvestrant in an injection volume of about 3.0 mL to about 5.0 mL, about 3.5 mL to about 4.5 mL, or about 4.0 mL.


In certain embodiments of the invention, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of fulvestrant pharmaceutical compositions of the invention is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of FASLODEX™, and the relative mean Cmax of fulvestrant pharmaceutical compositions of the invention is less than 80% of the relative mean Cmax of FASLODEX™. It is believed that such embodiments may provide benefits by providing a therapeutically effect amount of fulvestrant exposure to a subject while reducing the degree of one or more Cmax-driven side-effects or toxicities in comparison to the degree of side-effects or toxicities experienced by a subject from receiving a therapeutically effective amount of fulvestrant exposure from one or more dosages of FASLODEX™.


In some embodiments of the invention, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of fulvestrant pharmaceutical compositions of the invention is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of FASLODEX™, and the relative mean Cmax of fulvestrant pharmaceutical compositions of the invention is less than 80%, less than 75%, less than 70%, less than 65%, less than 60%, less than 55%, less than 50%, less than 45%, or less than 40% of the relative mean Cmax of FASLODEX™. In further embodiments, such fulvestrant pharmaceutical compositions are administered as a single intramuscular injection and comprise a dose of about 500 mg of fulvestrant at a concentration of about 100 mg/mL.


In yet further embodiments of the invention, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of fulvestrant pharmaceutical compositions of the invention is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of FASLODEX™, and the relative mean Cmax of fulvestrant pharmaceutical compositions of the invention is less than 80%, less than 75%, less than 70%, less than 65%, less than 60%, less than 55%, less than 50%, less than 45%, or less than 40% of the relative mean Cmax of FASLODEX™ in the fasting state. In further embodiments, such fulvestrant pharmaceutical compositions are administered as a single intramuscular injection and comprise a dose of about 500 mg of fulvestrant at a concentration of about 100 mg/mL.


In still further embodiments of the invention, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of fulvestrant pharmaceutical compositions of the invention is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of FASLODEX™, and the relative mean Cmax of fulvestrant pharmaceutical compositions of the invention is less than 80%, less than 75%, less than 70%, less than 65%, less than 60%, less than 55%, less than 50%, less than 45%, or less than 40% of the relative mean Cmax of FASLODEX™ in the fed state. In further embodiments, such fulvestrant pharmaceutical compositions are administered as a single intramuscular injection and comprise a dose of about 500 mg of fulvestrant at a concentration of about 100 mg/mL.


In some embodiments of the invention, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of fulvestrant pharmaceutical compositions of the invention is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of FASLODEX™, and the relative mean Cmax of fulvestrant pharmaceutical compositions of the invention is about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 90%, within about 45% to about 55%, within about 55% to about 65%, within about 65% to about 75%, within about 50% to about 60%, within about 60% to about 70%, or within about 70% to about 80% of the relative mean Cmax of FASLODEX™. In further embodiments, such fulvestrant pharmaceutical compositions are administered as a single intramuscular injection and comprise a dose of about 500 mg of fulvestrant at a concentration of about 100 mg/mL.


In yet further embodiments of the invention, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of fulvestrant pharmaceutical compositions of the invention is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of FASLODEX™, the relative mean Cmax of fulvestrant pharmaceutical compositions of the invention is about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 90%, within about 45% to about 55%, within about 55% to about 65%, within about 65% to about 75%, within about 50% to about 60%, within about 60% to about 70%, or within about 70% to about 80% of the relative mean Cmax of FASLODEX™ in the fasting state. In further embodiments, such fulvestrant pharmaceutical compositions are administered as a single intramuscular injection and comprise a dose of about 500 mg of fulvestrant at a concentration of about 100 mg/mL.


In still further embodiments of the invention, the 90% confidence intervals (CI) of the relative mean AUC(0-t), relative mean AUC(0-∞), or both of fulvestrant pharmaceutical compositions of the invention is within 80% to 125% of the relative mean AUC(0-t) and relative mean AUC(0-∞), respectively, of FASLODEX™, and the relative mean Cmax of fulvestrant pharmaceutical compositions of the invention is about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 90%, within about 45% to about 55%, within about 55% to about 65%, within about 65% to about 75%, within about 50% to about 60%, within about 60% to about 70%, or within about 70% to about 80% of the relative mean Cmax of FASLODEX™ in the fed state. In further embodiments, such fulvestrant pharmaceutical compositions are administered as a single intramuscular injection and comprise a dose of about 500 mg of fulvestrant at a concentration of about 100 mg/mL.


E. Methods of Treatment

In further embodiments, the invention is directed to methods of treatment comprising administration of a pharmaceutically effective amount of any of the fulvestrant pharmaceutical compositions described herein to a patient in need thereof. In particular embodiments, the invention is directed to a method of treating breast cancer, comprising administering a pharmaceutically acceptable amount of any of the fulvestrant pharmaceutical compositions described herein. In certain embodiments, the breast cancer is metastatic breast cancer. In other embodiments of the invention, the breast cancer is hormone receptor (HR)-positive breast cancer. In still other embodiments of the invention, the invention is directed to a method of treating hormone receptor (HR)-positive breast cancer in a post-menopausal woman comprising administration of a pharmaceutically effective amount of any of the fulvestrant pharmaceutical compositions described herein. In yet other embodiments, the invention is directed to a method of treating hormone receptor (HR)-positive breast cancer in a post-menopausal woman with disease progression following antiestrogen therapy comprising administration of a pharmaceutically effective amount of any of the fulvestrant pharmaceutical compositions described herein. In yet further embodiments, the invention is directed to a method of treating HR-positive, human epidermal growth factor receptor 2 (HER2)-negative advanced or metastatic breast cancer in a woman with disease progression after endocrine therapy.


In particular embodiments of the invention, a fulvestrant pharmaceutical composition as described herein is administered on days 1, 15, 29, and once monthly thereafter. In further embodiments of the invention, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered on days 1, 15, 29, and once monthly thereafter. In still further embodiments of the invention, a 250 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered on days 1, 15, 29, and once monthly thereafter.


In certain embodiments of the invention, a fulvestrant pharmaceutical composition as described herein is administered as a single injection. In other embodiments of the invention, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as a single injection. In yet other embodiments of the invention, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as a single 5 mL injection. In further embodiments of the invention, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as a single 4 mL injection. In yet further embodiments, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as a single 3 mL injection. In still other embodiments of the invention, a 250 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as a single injection. In further embodiments of the invention, a 250 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as a single 2.5 mL injection. In yet further embodiments of the invention, a 250 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as a single 5 mL injection.


In particular embodiments of the invention, a fulvestrant pharmaceutical composition as described herein is administered as two injections. In further embodiments of the invention, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as two injections. In still further embodiments of the invention, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as two 5 mL injections. In yet further embodiments of the invention, a 500 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as two 2 mL injections, two 2.5 mL injections, two 3 mL injections, two 3.5 mL injections, or two 4 mL injections. In other embodiments of the invention, a 250 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as two injections. In yet other embodiments of the invention, a 250 mg dose of any of the fulvestrant pharmaceutical compositions as described herein is administered as two 2.5 mL injections.


The fulvestrant pharmaceutical compositions described herein may be administered alone, or in combination with one or more additional therapeutic agents as defined herein. An additional therapeutic agent may be used to treat one or more core symptoms and/or comorbidities associated with cancer in general or breast cancer in particular. In one aspect, fulvestrant is formulated (and administered) with at least one therapeutic agent as a fixed dose. In another aspect, fulvestrant is formulated (and administered) separately from the therapeutic agent(s).


Some examples of therapeutic agents that may be used in combination with fulvestrant include, but are not limited to, e.g., a EGFR kinase inhibitor, a PDGFR kinase inhibitor, a FGFR kinase inhibitor, or any of the other cytotoxic, chemotherapeutic, antihormonal, anti-angiogenic, antiproliferative, pro-apoptotic, anti-HER2, radiation or a radiopharmaceutical, signal transduction inhibitors, or other anti-cancer agents or treatments. Examples of particular agents that can be used in combination with the fulvestrant pharmaceutical compositions of the disclosure include palbociclib, letrozole, anastrozole, doxorubicin, paclitaxel, docetaxel, vinorelbine, and 5-fluorouracil. In other embodiments, therapeutic agents that may be used in combination with fulvestrant include, but are not limited to, agents or treatments for one or more of pain, nausea, emesis, hot flushes, constipation, and dizziness.


Those skilled in the art will appreciate that numerous changes and modifications can be made to the preferred embodiments of the disclosure and that such changes and modifications can be made without departing from the spirit of the disclosure. It is, therefore, intended that the following examples and appended claims cover all such equivalent variations as fall within the true spirit and scope of the disclosure.


The disclosures of each patent, patent application, and publication cited or described in this document are hereby incorporated herein by reference, in its entirety.


EXAMPLES
Example: Preparation of Fulvestrant Pharmaceutical Compositions/Variants

Some exemplary fulvestrant pharmaceutical compositions were prepared with 50 mg/mL and 100 mg/mL concentrations of fulvestrant in aqueous suspensions. Tables 1-20 show aspects of the pharmaceutical compositions of the pharmaceutical compositions and the methods of preparation of some of the pharmaceutical compositions, also referred to as formulations, variants, or Lots in the Tables. Tables 4-7 and 23-27 and FIGS. 4-12 and 15 show aspects of the methods of preparation used to prepare some of the pharmaceutical compositions.


Where indicated in the Tables and Figures, the formulations B, E, I, J, K, L, L3F, L6, F003a, F003b, F003e, F004a, F003k2, F003k3, F005a2, F003l, F005b1, F015a1, F015a3, F005d1, F005c3, F005g5 tested in Studies 1-3 below were prepared via one or more of process steps of (1) low shear mixing, indicated in the Tables 23-27 and FIGS. 4-12 as “Mix” or “Mix with Vortex Mixer” steps; (2) high shear mixing, indicated as “HSM” or “Homogenize” steps; (3) high pressure homogenization, indicated as “HPH” or “Process with Nano DeBee” steps; (4) concentration via supernatant removal; and (5) application of sonication. Where indicated, supernatant removal was performed by phase separating the pharmaceutical composition and withdrawing the desired amount of supernatant to concentrate the suspensions to the target concentrations of fulvestrant, either 50 mg/mL or 100 mg/mL, depending on the pharmaceutical composition. Where indicated, phase separation was performed by overnight settling in a clear glass centrifuge tube. Application of centrifuge for phase separation could also be utilized.


Fulvestrant active pharmaceutical ingredient (which may also be referred to as “API” herein and in the Tables and Figures) was obtained in un-milled forms or in milled, micronized, or recrystallized forms from commercial suppliers. As-obtained particle size distributions for un-milled API varied from an LD Dv(90) of about 240 microns to an LD Dv(90) of about 2130 microns. As-obtained particle size distributions for milled, micronized, and recrystallized API varied from an LD Dv(90) of about 7 microns to an LD Dv(90) of about 18 microns. Fulvestrant API may be obtained in various particle size distributions from commercial sources and processed as described elsewhere herein to achieve the desired particle size distributions. Particle size distributions can be monitored throughout the processing steps through analysis of samples as described elsewhere herein.


Where indicated in the Tables and Figures, the formulations B, E, I, J, K, L, L3F, L6, F003a, F003b, F003e, F004a, F003k2, F003k3, F005a2, F003l, F005b1, F015a1, F015a3, F005d1, F005c3, F005g5 tested in Studies 1-3 below were prepared via high shear mixing (HSM) steps. The preparation of formulations can be performed with an IKA T10 Basic Disperser with an IKA S 10N-10G dispersing tool. At the speeds indicated (˜20,000 to 30,000 rpm), the mixture of fulvestrant and suspension vehicle was processed in cycles until the total processing time indicated was reached. Between each cycle, a formulation was vortexed at ˜3000 rpm for 30 seconds then sonicated for 1 minute to remove or reduce foam generated during the high shear mixing by the disperser. Formulations were also rested as needed in between cycles at room temperature to allow the disperser to cool down and avoid overheating of the product and the equipment. Sonication was performed with a Branson 3800 Ultrasonic Bath (Branson Ultrasonics Corp., Danbury, Conn.) at a frequency of 40 kHz. Other mixing and ultrasonic apparatuses may also be used to achieve mixing and particle size distribution as desired.


In some embodiments, high pressure homogenization was performed. In certain embodiments, high pressure homogenization (HPH) steps were performed with a Nano DeBEE High Pressure Homogenizer (BEE International, South Easton, Mass.) in a Labconco XPert Filtered Balance System (Model 3950630) (Labconco, Kansas City, Mo.), installed the 100 ml sample holder and Z5 nozzle in parallel flow configuration on Nano DeBEE High Pressure Homogenizer. The homogenizer was primed with filing water until the process pressure reached the processing pressure as indicated in the Tables and Figures. Water was removed from the system using the plunger to minimize the dilution of the batch by the residual priming water. Approximately ˜50 ml of the suspension for HPH processing was loaded from the 50 mL clear Pyrex glass bottle on Nano DeBEE High Pressure Homogenizer. The Nano DeBEE was run in continuous mode until the pressure reached the indicated target processing pressure. The suspension was then processed for the indicated number passes at the processing pressure. To avoid losing the prime of the system and consequently the processing pressure, only total ˜40 mL (8 strokes of ˜5 mL per stroke) of the suspension was processed and collected from each pass. The 40 mL suspension was then loaded back to the reservoir for the suspension to be processed in the next pass. After the processing was completed, 40 ml fine suspension was collected in a 100 mL clear Pyrex glass bottle by running Nano DeBEE High Pressure Homogenizer until no sample was pumped out. In certain embodiments, high pressure homogenization was performed with other apparatuses at processing pressures ranging from about 5,000 psi to about 45,000 psi. Other high pressure homogenization apparatuses may also be used to achieve the desired particle size distributions described herein.


Some formulations for Study 3 below were lyophilized and reconstituted with sterile water for injection, USP prior to administration, as indicated in the Example below.


References to “Assay” refers to high-performance liquid chromatography (HPLC) measurement of the fulvestrant concentration of the pharmaceutical composition at intermediate processing steps or in final result as prepared. The “Assay” results are given in absolute measured mg/mL or as a percentage (%) or (% LC), where percentages indicate the concentration of fulvestrant relative to the 50 mg/mL label claim of the commercially available FASLODEX™ product. Total impurities were also measured and are provided in the figures as a percentage by area (% a/a) where indicated. HPLC was performed with Agilent Technologies Agilent 1260 Infinity Quaternary LC module G1311B (Agilent Technologies, Santa Clara, Calif.). Other HPLC apparatuses may also be used to analyze the fulvestrant concentrations.


In some aspects, particle size and particle size distributions were analyzed with Malvern Mastersizer 3000 (Malvern Instruments Ltd., Malvern, Worcestershire, UK), with an attached sample dispersion unit with an in-line sonication probe for agglomerate dispersion prior to analysis via laser diffraction.


In some aspects, particle size and particle size distributions were analyzed with Malvern Morphologi G3 (Malvern Instruments Ltd., Malvern, Worcestershire, UK), to determine circle equivalent (CE) diameters via microscopy image capture and analysis.


Measurements of pH were obtained at ambient room temperature with a Thermo Scientific Orion Star A211 pH Meter (Thermo Fisher Scientific Inc., Waltham, Mass.).


Example: Pharmacokinetic Study 1 of Intramuscular Administration to Female Dogs

Fulvestrant pharmaceutical compositions B, E, I, J, K, and L were prepared as described elsewhere herein and in the Figures. A preclinical study was performed to determine the pharmacokinetics of the pharmaceutical compositions following a single intramuscular administration of 15.4 mg/kg to female dogs. The pharmacokinetics of 15.4 mg/kg IM FASLODEX™ (fulvestrant injection, 250 mg/5 mL) were also determined and used for comparison to the three prototype pharmaceutical compositions. The 15.4 mg/kg dose used in this study is the canine equivalent, in mg/m2, of the maximum dose (500 mg) for human use and was scaled for use in canine by dividing the dose (based on a 60 kg human) by a canine species conversion factor of 0.54.


Twenty-four non-naïve female beagle dogs were used in the study. The animals weighed between approximately 5-10 kg. Animal welfare for this study was in compliance with the U.S. Department of Agriculture's (USDA) Animal Welfare Act (9 Code of Federal Regulations (CFR) Parts 1, 2 and 3). The Guide for the Care and Use of Laboratory Animals, Institute of Laboratory Animal Resources, National Academy Press, Washington, D.C., was followed. The facility maintained an Animal Welfare Assurance statement with the National Institutes of Health, Office of Laboratory Animal Welfare.


The FASLODEX™ test articles contained a small molecule that was used as received and no adjustment was made for purity, salt correction, etc. The FASLODEX™ test articles were gently agitated prior to dispensing and dose delivery. Pharmaceutical Composition B, Pharmaceutical Composition E, Pharmaceutical Composition I, Pharmaceutical Composition J, Pharmaceutical Composition K, and Pharmaceutical Composition L were stored at room temperature and protected from light prior to use, and gently agitated prior to dispensing and dose delivery.


The animals were not fasted prior to dosing. Each animal received a single intramuscular (IM) dose of only one of the appropriate test article pharmaceutical compositions as outlined in the following study design table, Table 30. IM doses were administered with a 20 G needle via bolus injection into the same large muscle mass (using the Z-track injection technique) in the left hind limb of each animal. Attempts were made for consistent injections between animals [selection of the dose site (muscle), depth, etc.]. The hair was clipped from the injection site prior to dosing. The injection site was marked following dosing and remarked as necessary throughout the study. Specifications for all dose delivery were recorded and reported in the study report [including, but not limited to needle gauge/length, syringe size/barrel type with manufacturer and part number, estimated injection depth into the muscle, approximate duration required to administer the injection; any substantial resistance (either flow through the syringe/needle and/or into the muscle during administration)] was documented.














TABLE 30








Pharmaceutical







Composition







Fulvestrant
Dose
Dose




No of
Concentration
Level
Volume


Group
Test Article
Females
(mg/mL)
(mg/kg)
(mL/kg)




















1
FASLODEX ™
3
50
15.4
0.308


2
Pharmaceutical
3
50
15.4
0.308



Composition B






3
Pharmaceutical
3
50
15.4
0.308



Composition E






4
FASLODEX ™
3
50
15.4
0.308


5
Pharmaceutical
3
50
15.4
0.308



Composition I






6
Pharmaceutical
3
50
15.4
0.308



Composition J






7
Pharmaceutical
3
50
15.4
0.308



Composition K






8
Pharmaceutical
3
100
15.4
0.154



Composition L









All animals were observed at least twice a day for morbidity, mortality, injury, and availability of food and water. Any animals in poor health were identified for further monitoring and possible euthanasia.


Blood samples were collected at various time intervals to measure the blood plasma concentration of fulvestrant. Blood samples for Groups 1-3 were collected predose and at 0.25, 0.5, 1, 2, 4, 8, and 12 (on Day 1); and 24 (on Day 2), 48 (on Day 3), 120 (on Day 6), 192 (on Day 9), 264 (on Day 12), 336 (on Day 15), 384 (on Day 17), 456 (on Day 20), 528 (on Day 23), 600 (on Day 26), and 672 (on Day 29) hours postdose. Blood samples for Groups 4-8 were collected predose and at 0.25, 0.5, 1, 2, 4, 8, and 12 (on Day 1); and 24 (on Day 2), 48 (on Day 3), 72 (on Day 4), 96 (on Day 5), 120 (on Day 6), 192 (on Day 9), 264 (on Day 12), 336 (on Day 15), 384 (on Day 17), 528 (on Day 23), and 672 (on Day 29) hours postdose.


Whole venous blood samples of approximately 2 mL each were collected from a peripheral vein of all animals for determination of fulvestrant exposure. Blood was collected with sodium heparin anticoagulant (glass tube, no gel separator). All blood samples were placed on wet ice following collection until centrifuged. Blood was centrifuged at 3500 rpm for 7 minutes at 2 to 8° C. Plasma (minimum of 0.8 mL volume) was separated from blood cells within 0.75 hours of blood collection and frozen. Plasma samples were initially placed on dry ice prior to being stored in the appropriate freezer (−60 to −90° C.). Samples were shipped on dry ice for bioanalytical analysis.


A model independent method was used to determine Cmax and AUC values from fulvestrant plasma concentration-time data. Results are shown in Tables 31-37 and FIGS. 1B, 2A, 2C, and 3. Table 31 shows the pharmacokinetic data from the 15.4 mg/kg dosages as nominally dosed (based on the target fulvestrant concentration for each pharmaceutical composition). An “Assay %” is shown for the fulvestrant pharmaceutical compositions of the present disclosure used in the study. The “Assay %” represents the percentage equivalence of the particular pharmaceutical composition in comparison to the FASLODEX™ label claim fulvestrant concentration, with “Assay %” values determined via HPLC, measurement samples taken pre- and post-dose, with one value selected for normalization. The data in Tables 32-37 are normalized using the “Assay %” values to compare PK results based upon the actual mg/kg of fulvestrant administered, assuming linear scaling. FIGS. 1B, 2A, 2C, and 3 depict graphs of the dose normalized fulvestrant mean plasma concentrations.









TABLE 31







PK parameters based upon the nominal dose 15.4 mg/kg
















Assay (%)
Assay (%)






(measured
(measured






predose)
post-dose)











Variant (Geometric
Cmax
AUC0-14d
AUC0-28d
Starred value used for


Mean of n as indicated)
(ng/mL )
(hr * ng/mL)
(hr * ng/mL)
normalization















Faslodex
35.0
7015
8917




(LW466, n = 9)







Faslodex
45.7
7666
9306




(MB122, n = 6)







Faslodex
32.0
7177
9018




(MB948, n = 3)







Faslodex
36.9
8149
9817




(MC949, n = 4)







Faslodex
37.5
7408
9195




(All, n = 22)







B (n = 3)
8.7
1930
3250
100.0*
138.9


E (n = 3)
29.1
5750
8380
93.4*
91.8


I (n = 3)
41.5
8840
12300
95.6*
99.6


J (n = 3)
44.8
5750
8100
87.6*
93.6


K (n = 3)
69.7
7540
9630
84.6*
91.2


L (n = 3)
63.9
8430
11000
94.1*
97.3


L3F (n = 3)
22.6
5140
7130
83.8*
79.0


L6 (n = 3)
24.7
6050
9360
113.9*
113.9


F003a (n = 3)
27.7
5860
8610
95.0*
97.1


F003b (n = 3)
32.5
7210
9650
96.3*



F003e (n = 3)
28.5
6400
9080
100.6*
100.5


F004a (n = 3)
31.7
4310
6190
99.8*
100.4


F003k2 (n = 4)
33
3910
5960
97.8*
100.1


F003k3 (n = 4)
26.8
5430
7060
99.6*
100.7


F005a2 (L, n = 3)
19.7
4370
6840

93.2*


F003l (L, n = 3)
25.1
5510
8680

99.2*


F005b1 (n = 3)
49.7
9420
12100
100.2*



F015a1 (n = 3)
63.6
4750
7120
103.8*



F015a3 (L, n = 3)
34.4
3850
6000

98.6*


F005d1 (n = 3)
37.9
7180
9910
100.5*
99.2


F005c3 (L, n = 3)
17.7
3680
5820
95.2*

















TABLE 32







PK parameters normalized against the actual dose












Variant
Cmax
AUC0-14d
AUC0-28d



(Geometric Mean
(ng/mL
(hr * ng/mL
(hr * ng/mL



of n as indicated)
per mg/kg)
per mg/kg)
per mg/kg)
















Faslodex
2.3
456
579



(LW466, n = 9)






Faslodex
3.0
498
604



(MB122, n = 6)






Faslodex
2.1
466
586



(MB948, n = 3)






Faslodex
2.4
529
637



(MC949, n = 4)






Faslodex
2.4
481
597



(All, n = 22)






B (n = 3)
0.6
125
211



E (n = 3)
2.0
400
583



I (n = 3)
2.8
600
835



J (n = 3)
3.3
426
600



K (n = 3)
5.3
579
739



L (n = 3)
4.4
582
759



L3F (n = 3)
1.8
398
552



L6 (n = 3)
1.4
345
534



F003a (n = 3)
1.9
401
589



F003b (n = 3)
2.2
486
651



F003e (n = 3)
1.8
413
586



F004a (n = 3)
2.1
280
403



F003k2 (n = 4)
2.2
260
396



F003k3 (n = 4)
1.7
354
460



F005a2 (L, n = 3)
1.4
304
477



F003l (L, n = 3)
1.6
361
568



F005b1 (n = 3)
3.2
610
784



F015a1 (n = 3)
4.0
297
445



F015a3 (L, n = 3)
2.3
254
395



F005d1 (n = 3)
2.4
464
640



F005c3 (L, n = 3)
1.2
251
397

















TABLE 33







Comparison of normalized PK parameters against all Faslodex lots










Variant
Cmax
AUC0-14d
AUC0-28d


(Geometric Mean
ratio to
ratio to
ratio to


of n as indicated)
Faslodex (%)
Faslodex (%)
Faslodex (%)













Faslodex
93
95
97


(LW466, n = 9)





Faslodex
122
103
101


(MB122, n = 6)





Faslodex
85
97
98


(MB948, n = 3)





Faslodex
98
110
107


(MC949, n = 4)





Faslodex
100
100
100


(All, n = 22)





B (n = 3)
23
26
35


E (n = 3)
83
83
98


I (n = 3)
116
125
140


J (n = 3)
136
89
101


K (n = 3)
219
120
124


L (n = 3)
181
121
127


L3F (n = 3)
72
83
93


L6 (n = 3)
58
72
89


F003a (n = 3)
78
83
99


F003b (n = 3)
90
101
109


F003e (n = 3)
75
86
98


F004a (n = 3)
85
58
67


F003k2 (n = 4)
90
54
66


F003k3 (n = 4)
72
74
77


F005a2 (L, n = 3)
56
63
80


F003l (L, n = 3)
67
75
95


F005b1 (n = 3)
132
127
131


F015a1 (n = 3)
163
62
75


F015a3 (L, n = 3)
93
53
66


F005d1 (n = 3)
100
96
107


F005c3 (L, n = 3)
50
52
66
















TABLE 34







Comparison of normalized PK parameters against Faslodex


lot LW466










Variant
Cmax
AUC0-14d
AUC0-28d


(Geometric Mean
ratio to
ratio to
ratio to


of n as indicated)
Faslodex (%)
Faslodex (%)
Faslodex (%)













Faslodex
100
100
100


(LW466, n = 9)





Faslodex
131
109
104


(MB122, n = 6)





Faslodex
92
102
101


(MB948, n = 3)





Faslodex
106
116
110


(MC949, n = 4)





Faslodex
107
106
103


(All, n = 22)





B (n = 3)
25
28
36


E (n = 3)
89
88
101


I (n = 3)
124
132
144


J (n = 3)
146
94
104


K (n = 3)
236
127
128


L (n = 3)
194
128
131


L3F (n = 3)
77
87
95


L6 (n = 3)
62
76
92


F003a (n = 3)
83
88
102


F003b (n = 3)
97
107
112


F003e (n = 3)
81
91
101


F004a (n = 3)
91
62
70


F003k2 (n = 4)
97
57
68


F003k3 (n = 4)
77
78
79


F005a2 (L, n = 3)
60
67
82


F003l (L, n = 3)
72
79
98


F005b1 (n = 3)
142
134
135


F015a1 (n = 3)
175
65
77


F015a3 (L, n = 3)
100
56
68


F005d1 (n = 3)
108
102
111


F005c3 (L, n = 3)
53
55
69
















TABLE 35







Comparison of normalized PK parameters against Faslodex


lot MB122










Variant
Cmax
AUC0-14d
AUC0-28d


(Geometric Mean
ratio to
ratio to
ratio to


of n as indicated)
Faslodex (%)
Faslodex (%)
Faslodex (%)













Faslodex
76
92
96


(LW466, n = 9)





Faslodex
100
100
100


(MB122, n = 6)





Faslodex
70
94
97


(MB948, n = 3)





Faslodex
81
106
105


(MC949, n = 4)





Faslodex
82
97
99


(All, n = 22)





B (n = 3)
19
25
35


E (n = 3)
68
80
96


I (n = 3)
95
121
138


J (n = 3)
112
86
99


K (n = 3)
180
116
122


L (n = 3)
148
117
126


L3F (n = 3)
59
80
91


L6 (n = 3)
47
69
88


F003a (n = 3)
64
80
97


F003b (n = 3)
74
98
108


F003e (n = 3)
62
83
97


F004a (n = 3)
69
56
67


F003k2 (n = 4)
74
52
65


F003k3 (n = 4)
59
71
76


F005a2 (L, n = 3)
46
61
79


F003l (L, n = 3)
55
72
94


F005b1 (n = 3)
108
123
130


F015a1 (n = 3)
134
60
74


F015a3 (L, n = 3)
76
51
65


F005d1 (n = 3)
82
93
106


F005c3 (L, n = 3)
41
50
66
















TABLE 36







Comparison of normalized PK parameters against Faslodex


lot MB948










Variant
Cmax
AUC0-14d
AUC0-28d


(Geometric Mean
ratio to
ratio to
ratio to


of n as indicated)
Faslodex (%)
Faslodex (%)
Faslodex (%)













Faslodex
109
98
99


(LW466, n = 9)





Faslodex
143
107
103


(MB122, n = 6)





Faslodex
100
100
100


(MB948, n = 3)





Faslodex
115
114
109


(MC949, n = 4)





Faslodex
117
103
102


(All, n = 22)





B (n = 3)
27
27
36


E (n = 3)
97
86
99


I (n = 3)
136
129
143


J (n = 3)
160
91
103


K (n = 3)
257
124
126


L (n = 3)
212
125
130


L3F (n = 3)
84
85
94


L6 (n = 3)
68
74
91


F003a (n = 3)
91
86
100


F003b (n = 3)
105
104
111


F003e (n = 3)
89
89
100


F004a (n = 3)
99
60
69


F003k2 (n = 4)
105
56
68


F003k3 (n = 4)
84
76
79


F005a2 (L, n = 3)
66
65
81


F003l (L, n = 3)
79
77
97


F005b1 (n = 3)
155
131
134


F015a1 (n = 3)
191
64
76


F015a3 (L, n = 3)
109
54
67


F005d1 (n = 3)
118
100
109


F005c3 (L, n = 3)
58
54
68
















TABLE 37







Comparison of normalized PK parameters against Faslodex


lot MB949










Variant
Cmax
AUC0-14d
AUC0-28d


(Geometric Mean
ratio to
ratio to
ratio to


of n as indicated)
Faslodex (%)
Faslodex (%)
Faslodex (%)













Faslodex
95
86
91


(LW466, n = 9)





Faslodex
124
94
95


(MB122, n = 6)





Faslodex
87
88
92


(MB948, n = 3)





Faslodex
100
100
100


(MC949, n = 4)





Faslodex
102
91
94


(All, n = 22)





B (n = 3)
24
24
33


E (n = 3)
84
76
91


I (n = 3)
118
113
131


J (n = 3)
139
81
94


K (n = 3)
223
109
116


L (n = 3)
184
110
119


L3F (n = 3)
73
75
87


L6 (n = 3)
59
65
84


F003a (n = 3)
79
76
92


F003b (n = 3)
91
92
102


F003e (n = 3)
77
78
92


F004a (n = 3)
86
53
63


F003k2 (n = 4)
91
49
62


F003k3 (n = 4)
73
67
72


F005a2 (L, n = 3)
57
58
75


F003l (L, n = 3)
69
68
89


F005b1 (n = 3)
134
115
123


F015a1 (n = 3)
166
56
70


F015a3 (L, n = 3)
94
48
62


F005d1 (n = 3)
102
88
100


F005c3 (L, n = 3)
50
47
62









Example: Pharmacokinetic Study 2 of Intramuscular Administration to Female Dogs

Fulvestrant pharmaceutical compositions L3F and L6 were prepared as described elsewhere herein and in the Figures. A preclinical study was performed to determine the pharmacokinetics of the pharmaceutical compositions following a single intramuscular administration of 15.4 mg/kg to female dogs. The pharmacokinetics of 15.4 mg/kg IM FASLODEX™ (fulvestrant injection, 250 mg/5 mL) were also determined and used for comparison to the three prototype pharmaceutical compositions. The 15.4 mg/kg dose used in this study is the canine equivalent, in mg/m2, of the maximum dose (500 mg) for human use and was scaled for use in canine by dividing the dose (based on a 60 kg human) by a canine species conversion factor of 0.54.


Nine non-naïve female beagle dogs were used in the study. The animals weighed between approximately 5-13 kg. Animal welfare for this study was in compliance with the U.S. Department of Agriculture's (USDA) Animal Welfare Act (9 Code of Federal Regulations (CFR) Parts 1, 2 and 3). The Guide for the Care and Use of Laboratory Animals, Institute of Laboratory Animal Resources, National Academy Press, Washington, D.C., was followed. The facility maintained an Animal Welfare Assurance statement with the National Institutes of Health, Office of Laboratory Animal Welfare.


The FASLODEX™ test articles contained a small molecule that was used as received and no adjustment was made for purity, salt correction, etc. The FASLODEX™ test articles were gently agitated prior to dispensing and dose delivery. Pharmaceutical Compositions L3F and L6 were stored at room temperature and protected from light prior to use, and gently agitated prior to dispensing and dose delivery.















TABLE 38










Fulvestrant
Dose



Dose

Dosage
Conc.
Volume



Group
Test Article
(mg/kg)
(mg/mL)
(mL/kg)






















1
FASLODEX ™
15.4
 50
0.308



2
Pharmaceutical
15.4
100
0.154




Composition







L3F






3
Pharmaceutical
15.4
100
0.154




Composition







L6










The animals were not fasted prior to dosing. Each animal received a single intramuscular (IM) dose of only one of the appropriate test article pharmaceutical compositions as outlined in the following study design table, Table 38. IM doses were administered with a 20 G needle via bolus injection into the same large muscle mass (using the Z-track injection technique) in the left hind limb of each animal. Attempts were made for consistent injections between animals [selection of the dose site (muscle), depth, etc.]. The hair was clipped from the injection site prior to dosing. The injection site was marked following dosing and remarked as necessary throughout the study. Specifications for all dose delivery were recorded and reported in the study report [including, but not limited to needle gauge/length, syringe size/barrel type with manufacturer and part number, estimated injection depth into the muscle, approximate duration required to administer the injection; any substantial resistance (either flow through the syringe/needle and/or into the muscle during administration)] was documented.


All animals were observed at least twice a day for morbidity, mortality, injury, and availability of food and water. Any animals in poor health were identified for further monitoring and possible euthanasia.


Whole venous blood samples of approximately 2 mL each were collected from a peripheral vein of all animals for determination of fulvestrant exposure. Samples were collected at the following target timepoints; predose, 0.25, 0.5, 1,2, 4, 8, 12, 24 (Day 2), 48 (Day 3), 72 (Day 4), 96 (Day 5), 120 (Day 6), 192 (Day 9), 264 (Day 12), 336 (Day 15), 384 (Day 17), 528 (Day 23), and 672 (Day 29) hours after administration. Blood was collected with sodium heparin anticoagulant (glass tube, no gel separator). All blood samples were placed on wet ice following collection until centrifuged. Blood was centrifuged at 3500 rpm for 7 minutes at 2 to 8° C. Plasma (minimum of 0.8 mL volume) was separated from blood cells within 0.75 hours of blood collection and frozen. Plasma samples were initially placed on dry ice prior to being stored in the appropriate freezer (−60 to −90° C.). Samples were shipped on dry ice for bioanalytical analysis.


A model independent method was used to determine Cmax and AUC values from fulvestrant plasma concentration-time data. Results are shown in Tables 31-37 and FIGS. 2A and 2C. Table 31 shows the pharmacokinetic data from the 15.4 mg/kg dosages as nominally dosed (based on the target fulvestrant concentration for each pharmaceutical composition). An “Assay %” is shown for the fulvestrant pharmaceutical compositions of the present disclosure used in the study. The “Assay %” represents the percentage equivalence of the particular pharmaceutical composition in comparison to the FASLODEX™ label claim fulvestrant concentration, with “Assay %” values determined via HPLC, measurement samples taken pre- and post-dose, with one value selected for normalization. The data in Tables 32-37 are normalized using the “Assay %” values to compare PK results based upon the actual mg/kg of fulvestrant administered, assuming linear scaling. FIGS. 2A and 2C depict graphs of the dose normalized fulvestrant mean plasma concentrations.


Example: Pharmacokinetic Study 3 of Intramuscular and Intravenous Administration to Female Dogs

Fulvestrant formulations F003a, F003b, F004a, F003e, F003k2, F003k3, F005a2, F003l, F005b1, F015a1, F005d1, F005c3, F015a3, F005g5, Del-1S, Del-2S, F005H3, Lot 15, Lot 26, Lot 27, Lot 28, Lot 42, Lot 43, Lot 45, Lot 46, Lot 47, and Lot 48 were prepared as described elsewhere herein and in the Figures. In some instances, the formulations were prepared using different processes as indicated, referred to by an alphanumeric process identifier, such as “Process A1,” “Process A2,” and the like. A fulvestrant pharmaceutical composition for intravenous injection, referred to as batch FV-004/15M, was prepared as described below. A preclinical study was performed to determine the pharmacokinetics of the pharmaceutical compositions following a single intramuscular (IM) administration of 15.4 mg/kg to female dogs. The pharmacokinetics of 15.4 mg/kg IM FASLODEX™ (fulvestrant injection, 250 mg/5 mL) were also determined and used for comparison to the three prototype pharmaceutical compositions. The 15.4 mg/kg dose used in this study is the canine equivalent, in mg/m2, of the maximum dose (500 mg) for human use and was scaled for use in canine by dividing the dose (based on a 60 kg human) by a canine species conversion factor of 0.54.


One hundred fifty-six non-naïve female beagle dogs of body weight range of 5.65 to 11.40 kilograms were used in the study and assigned to Groups 1-48, as shown in Table 39 below.


Animal welfare for this study was in compliance with the U.S. Department of Agriculture's (USDA) Animal Welfare Act (9 Code of Federal Regulations (CFR) Parts 1, 2 and 3). The Guide for the Care and Use of Laboratory Animals, Institute of Laboratory Animal Resources, National Academy Press, Washington, D.C., was followed. The facility maintained an Animal Welfare Assurance statement with the National Institutes of Health, Office of Laboratory Animal Welfare.















TABLE 39







Number

Fulvestrant
Dose
Dose


Group

of
Dose
Concentration
Level
Volume


Number
Test Article
Females
Route
(mg/mL)
(mg/kg)
(mL/kg)







 1
Faslodex (lot LW466)
3
IM
 50
15.4 
0.308


 2
Faslodex (lot MB122)
3
IM
 50
15.4 
0.308


 3
Faslodex (lot MB948)
3
IM
 50
15.4 
0.308


 4
Formulation F003a
3
IM
100
15.4 
0.154


 5
Formulation F003b
3
IM
100
15.4 
0.154


 6
Formulation F004a
3
IM
100
15.4 
0.154


 7
Formulation F003e
3
IM
100
15.4 
0.154


 8
Formulation F003k2
4
IM
100
15.4 
0.154


 9
Formulation F003k3
4
IM
100
15.4 
0.154


10
Faslodex (lot MC949)
4
IM
 50
15.4 
0.308


11
Formulation F005a2
3
IM
100
15.4 
0.154


12
Formulation F003l
4
IM
100
15.4 
0.154


13
Formulation F005b1
3
IM
100
15.4 
0.154


14
Formulation F015a1
3
IM
100
15.4 
0.154


15
Formulation F005d1
3
IM
100
15.4 
0.154


16
Formulation F005c3
4
IM
100
15.4 
0.154


17
Formulation F015a3
3
IM
100
15.4 
0.154


18
Fulvestrant
4
IV
 20
2.5
0.125



(batch FV-004/15 M)







19
Formulation F005g5
4
IM
100
15.4 
0.154


20
Formulation Del-1S
4
IM
100
15.4 
0.154


21
Formulation Del-2S
4
IM
100
15.4 
0.154


22
Formulation F005H3
3
IM
100
15.4 
0.154


23
Lot 15, by Process E1
4
IM
100
15.4 
0.154


24
Lot 15, by Process E2
3
IM
100
15.4 
0.154


25
Lot 26, by Process F1
3
IM
100
15.4 
0.154


26
Lot 26, by Process F2
3
IM
100
15.4 
0.154


27
Lot 26, by Process F3
3
IM
100
15.4 
0.154


28
Lot 26, by Process F4
3
IM
100
15.4 
0.154


29
Lot 26, by Process J1
3
IM
100
15.4 
0.154


30
Lot 26, by Process J2
3
IM
100
15.4 
0.154


31
Lot 26, by Process J3
3
IM
100
15.4 
0.154


32
Lot 26, by Process J4
3
IM
100
15.4 
0.154


33
Lot 42, by Process G1
3
IM
100
15.4 
0.154


34
Lot 42, by Process G2
3
IM
100
15.4 
0.154


35
Lot 43, by Process H1
3
IM
100
15.4 
0.154


36
Lot 43, by Process H2
3
IM
100
15.4 
0.154


37
Lot 27, by Process A1
3
IM
100
15.4 
0.154


38
Lot 27, by Process A2
3
IM
100
15.4 
0.154


39
Lot 27, by Process A3
3
IM
100
15.4 
0.154


40
Lot 27, by Process A4
3
IM
100
15.4 
0.154


41
Lot 28, by Process B1
3
IM
100
15.4 
0.154


42
Lot 28, by Process B2
3
IM
100
15.4 
0.154


43
Lot 28, by Process B3
3
IM
100
15.4 
0.154


44
Lot 28, by Process B4
3
IM
100
15.4 
0.154


45
Lot 45, by Process C1
3
IM
100
15.4 
0.154


46
Lot 46
3
IM
100
15.4 
0.154


47
Lot 47
3
IM
100
15.4 
0.154


48
Lot 48
3
IM
100
15.4 
0.154









Pharmaceutical Compositions F003a, F003b, F004a, F003e, F003k2, F003k3, F005a2, F003l, F005b1, F015a1, F005d1, F005c3, F015a3, FV-004/15M, Del-1S, and Del-2S were stored at room temperature and protected from light prior to use, and gently agitated via inversion prior to dispensing and dose delivery. If visible clumps of material were seen on the vial inside wall or inner seal of the vial cap after 3 minutes of inversion, the tightly capped vial was vortexed at moderate intensity and unlimited duration until clumps were not visible. FASLODEX™ was supplied as two 5-mL clear neutral glass (Type 1) syringe barrels, each containing a 250 mg/5 mL (50 mg/mL) solution for intramuscular injection. Upon receipt, FASLODEX™ was stored refrigerated (2°−8° C.) and protected from light. The procedure to prepare and administer FASLODEX™ was performed as outlined in the manufacturer's prescribing information.


Lyophilized pharmaceutical compositions of formulations F005g5, F005H3, F015a3, Lot 15, Lot 26, Lot 27, Lot 28, Lot 42, Lot 43, Lot 45, Lot 46, Lot 47, and Lot 48 were reconstituted prior to dosing. Using an empty syringe and hypodermic needle, about 5 mL of air was withdrawn from the head space of the vial (above the lyophilized contents) via the septum and the syringe and needle were discarded. Using a sterile syringe and hypodermic needle, 5 mL of sterile water for injection, USP were added to the vial by piercing the septum and injecting a stream of water slowly around the inner wall of the neck of the vial to wet the lyophilized cake without touching any of the vial contents. The needle was removed from the septum and the vial was gently swirled until a visually homogeneous particulate suspension formed, with no visual clumps or material attached to the inside wall of the vial. If a homogeneous suspension was not formed after 5 minutes of swirling, the vial was vortexed until a homogeneous suspension was formed. The vials were not shaken to avoid generating bubbles or excessive foam.


Group 18 was administered an intravenous batch of fulvestrant (batch FV-004/15M) prepared as follows by (% w/v): 2% fulvestrant, 10% EtOH, 79% propylene glycol, 1% Poloxamer 407, 8% Water for Injection, USP. Fulvestrant API was stored at 2-8° C., protected from light. Care was taken to protect the API from humidity during weighing. Fulvestrant powder was dissolved in ethanol and swirled and vortexed as needed to dissolve completely. Propylene glycol was added and mixed to dissolve to a clear liquid state. Poloxamer 407 was dissolved in water for injection, USP in a separate vessel and mixed, vortexed, and sonicated as needed to dissolve into to a clear liquid state. The Poloxamer 407 in water for injection solution was added to the fulvestrant/ethanol solution. Propylene glycol was added and the solution was mixed and vortexed to achieve a clear liquid. The solution was filtered through a 0.2 μm or 0.22 μm syringe (to ensure that all liquid volume was usable) tip filter (PVDF) into a clear glass vessel. The prepared formulation as stored at room temperature for up to four hours prior to dosing under protection from light exposure. Intravenous doses were administered via the cephalic (or other suitable) vein as a slow injection over approximately 1 minute. Batch FV-004/15M was administered intravenously at a dose of 2.5 mg/kg.


The animals were not fasted prior to dosing. Each animal in Groups 4-9, 11-17, and 19-48 received a single intramuscular (IM) dose of only one of the appropriate test article pharmaceutical compositions as outlined in Table 39. IM doses were administered with a 20 G needle via bolus injection into the same large muscle mass (using the Z-track injection technique) in the left hind limb of each animal. Attempts were made for consistent injections between animals [selection of the dose site (muscle), depth, etc.]. The hair was clipped from the injection site prior to dosing. The injection site was marked following dosing and remarked as necessary throughout the study. Specifications for all dose delivery were recorded and reported in the study report [including, but not limited to needle gauge/length, syringe size/barrel type with manufacturer and part number, estimated injection depth into the muscle, approximate duration required to administer the injection; any substantial resistance (either flow through the syringe/needle and/or into the muscle during administration)] was documented. Animals in Groups 13-17 and 19-48 were administered 1 tablet or capsule (25 mg) of (PO) diphenhydramine at approximately 1 hour prior to dosing.


All animals were observed at least twice a day for morbidity, mortality, injury, and availability of food and water. Any animals in poor health were identified for further monitoring and possible euthanasia.


Whole venous blood samples of approximately 2 mL each were collected from a peripheral vein of all animals for determination of fulvestrant exposure. Blood samples for Groups 1-7 were collected predose and at 0.25, 0.5, 1, 2, 4, 8, and 12 (on Day 1); and 24 (on Day 2), 48 (on Day 3), 72 (on Day 4), 96 (on Day 5), 120 (on Day 6), 192 (on Day 9), 264 (on Day 12), 336 (on Day 15), 384 (on Day 17), 528 (on Day 23), and 672 (on Day 29) hours postdose. Blood samples for Groups 8-14 were collected predose and at 0.25, 0.5, 1, 2, 4, 8, and 12 (on Day 1); and 24 (on Day 2), 48 (on Day 3), 72 (on Day 4), 96 (on Day 5), 120 (on Day 6), 192 (on Day 9), 264 (on Day 12), 336 (on Day 15), 384 (on Day 17), 456 (on Day 20), 528 (on Day 23), 600 (on Day 26), 672 (on Day 29), 696 (Day 30), 768 (Day 33), 816 (Day 35), 864 (Day 37), 936 (Day 40) and 1008 (Day 43) hours post-dose. Blood samples for Groups 15-17 and 19-21 were collected predose and at 0.25, 0.5, 1, 2, 4, 8, 12 (Day 1), 24 (Day 2), 48 (Day 3), 72 (Day 4), 96 (Day 5), 120 (Day 6), 192 (Day 9), 264 (Day 12), 336 (Day 15), 384 (Day 17), 456 (Day 20), 528 (Day 23), 600 (Day 26), 672 (Day 29), 696 (Day 30), 768 (Day 33), 816 (Day 35), 864 (Day 37), 936 (Day 40), 1008 (Day 43), and 1176 (Day 50) hours postdose. Blood samples for Group 18 were collected predose and at 0.033 (2 minutes), 0.1 (6 minutes), 0.13 (8 minutes), 0.27 (16 minutes), 0.52 (31 minutes), 0.77 (46 minutes), 1, 2, 3, 4, 6, 8, 10, and 12 hours postdose on Day 1 and at 24 (on Day 2), 30 (on Day 2), 48 (on Day 3) and 72 (on Day 4) hours postdose, with postdose measurements from the start of dose administration, which took about 1 minute to complete. Blood samples for Groups 22-48 were collected predose and at 0.25, 0.5, 1, 2, 4, 8, 12 (Day 1), 24 (Day 2), 48 (Day 3), 72 (Day 4), 96 (Day 5), 120 (Day 6), 144 (Day 7), 168 (Day 8), 192 (Day 9), 216 (Day 10), 240 (Day 11), 264 (Day 12), 336 (Day 15), 384 (Day 17), 456 (Day 20), 528 (Day 23), 600 (Day 26), 672 (Day 29), 696 (Day 30), 768 (Day 33), 816 (Day 35), 864 (Day 37), 936 (Day 40), 1008 (Day 43), and 1176 (Day 50) hours postdose. Blood was collected with sodium heparin anticoagulant (glass tube, no gel separator). All blood samples were placed on wet ice following collection until centrifuged. Blood was centrifuged at 3500 rpm for 7 minutes at 2 to 8° C. Plasma (minimum of 0.8 mL volume) was separated from blood cells within 0.75 hours of blood collection and frozen. Plasma samples were initially placed on dry ice prior to being stored in the appropriate freezer (−60 to −90° C.). Samples were shipped on dry ice for bioanalytical analysis to determine absolute ng/mL fulvestrant in the plasma.













TABLE 40











PK parameters based upon the






Faslodex lots based upon the


Formulation



nominal dose 15.4 mg/kg











(Geometric Mean,
PK parameters compared to
Cmax
AUC0-14 d
AUC0-28 d


n = 3 unless
nominal dose 15.4 mg/kg
ratio to
ratio to
ratio to













indicated
Cmax
AUC0-14 d
AUC0-28 d
Faslodex
Faslodex
Faslodex


otherwise)
(ng/mL)
(hr*ng/mL)
(hr*ng/mL)
(%)
(%)
(%)





Faslodex (All, n = 22)
37.5
7408
 9195
100
100
100


F005g5
32.1
6950
10400
 86
 94
113


Lot 15, by Process E1
20.1
3890
 5500
 54
 53
 60


Lot 15, by Process E2
20.3
4190
 6230
 54
 57
 68


Lot 26, by Process F1
19.5
4150
 6650
 52
 56
 72


Lot 26, by Process F2
30.5
5510
 7850
 81
 74
 85


Lot 26, by Process F3
25.7
5350
 8260
 68
 72
 90


Lot 26, by Process F4
30.8
7210
10200
 82
 97
111


Lot 26, by Process J1
25.2
5490
 7910
 67
 74
 86


Lot 26, by Process J2
20.8
4640
 7190
 55
 63
 78


Lot 26, by Process J3
21.1
4720
 7310
 56
 64
 80


Lot 26, by Process J4
21.3
4320
 5900
 57
 58
 64


Lot 42, by Process G1
28.1
4640
 7410
 75
 63
 81


Lot 42, by Process G2
33.8
6110
 8800
 90
 82
 96


Lot 43, by Process H1
25.0
5190
 7500
 67
 70
 82


Lot 43, by Process H2
22.2
4430
 6250
 59
 60
 68


Lot 27, by Process A1
92.6
6150
 8710
247
 83
 95


Lot 27, by Process A2
27.9
6240
 9170
 74
 84
100


Lot 27, by Process A3
26.3
5100
 7680
 70
 69
 84


Lot 27, by Process A4
29.1
6030
 8620
 78
 81
 94


Lot 28, by Process B1
21.9
3950
 6230
 58
 53
 68


Lot 28, by Process B2
36.3
7010
 9870
 97
 95
107


Lot 28, by Process B3
31.6
6880
 9660
 84
 93
105


Lot 28, by Process B4
31.0
6330
 9000
 83
 85
 98


Lot 45, by Process C1
29.8
5320
 8560
 79
 72
 93


Lot 46
30.2
5570
 8240
 80
 75
 90


Lot 47
27.9
5230
 8070
 74
 71
 88


Lot 48
26.3
4900
 7410
 70
 66
 81









A model independent method was used to determine Cmax and AUC values from fulvestrant plasma concentration-time data. Results are shown in Tables 31-37 and 40 and FIGS. 1A, 1B, 2A, 2B, 2C, 13, and 14. Table 31 shows the pharmacokinetic data from the 15.4 mg/kg dosages as nominally dosed (based on the target fulvestrant concentration for each pharmaceutical composition). An “Assay %” is shown in Table 31 for the fulvestrant pharmaceutical compositions of the present disclosure used in the study. The “Assay %” represents the percentage equivalence of the particular pharmaceutical composition in comparison to the FASLODEX™ label claim fulvestrant concentration, with “Assay %” values determined via HPLC, measurement samples taken pre- and post-dose, with one value selected for normalization. The data in Tables 32-37 are normalized using the “Assay %” values to compare PK results based upon the actual mg/kg of fulvestrant administered, assuming linear scaling. FIGS. 1A, 1B, 2A, 2B, and 2C depict graphs of the dose normalized fulvestrant mean plasma concentrations. Table 40 shows the pharmacokinetic data from the 15.4 mg/kg dosages as nominally dosed (based on the target fulvestrant concentration for each pharmaceutical composition) in comparison to the geometric mean of all Faslodex lots tested (n=22). FIGS. 13 and 14 depict fulvestrant plasma measurements for administration of Faslodex Lot MB948 to three female dogs and administration of fulvestrant formulation Lot 27 processed by Process A2 to three female dogs (referred to in FIG. 14 as subjects 924, 925, and 926).


Example: Microscopic Imaging of Fulvestrant Particles in Suspensions

Some exemplary fulvestrant pharmaceutical compositions of the present disclosure were examined via optical and scanning electron microscopy. Suspensions of fulvestrant pharmaceutical compositions Variants B, E, I, J, K, L, L3F, L6, F003a, F003b, F004a, F003e, F00k2, and F003k3 were examined via optical microscopy. Optical microscopy was performed at 400× magnification with a polarized light filter using fully dispersed homogeneous suspension samples.


Example: Particle Size Distribution Characterization of Fulvestrant Pharmaceutical Compositions

Batches of fulvestrant pharmaceutical composition Lot 27, described elsewhere herein, were prepared by the methods of preparation 101 of FIG. 15. Samples were taken periodically during high shear mixing, prior to any high pressure homogenization steps. Some test samples, referred to as “Sample 1”, were taken after approximately five hours of high shear mixing and other test samples, referred to as “Sample 2”, were taken after approximately 13.7 hours to high shear mixing. Particle sizes of test samples were analyzed using optical microscopy with a Malvern Morphologi G3 apparatus for microscopy image capture and analysis. CE diameters were measured and number-weighted and volume-weighted particle size distribution parameters were determined as shown in Tables 41 and 42. The CE diameter ranges of measurement aliquots are also shown, with the lower range value of 0.54 microns representing the lower limit of detection for the apparatus setup. Test samples were analyzed with a Malvern Mastersizer 3000 apparatus for laser diffraction particle size characterization of LD diameters.









TABLE 41







Volume-Weighted Distribution Parameters


















Circle









Equivalent






CE
CE
CE
(CE)-
LD
LD
LD



Dv (10)
Dv (50)
Dv (90)
diameter-
Dv10
Dv50
Dv90


Formulation
(μm)
(μm)
(μm)
range (μm)
(μm)
(μm)
(μm)





Lot 27 (Sample 1)
6.113
13.77
32.71
0.54-49.72
1.81
6.68
16.6


Lot 27 (Sample 1)
6.509
14.34
28.64
0.54-54.14
1.85
6.93
17.7


Lot 27 (Sample 1)
6.378
12.76
23.90
0.54-55.04





Lot 27 (Sample 1)
5.297
10.73
24.57






Lot 27 (Sample 1)
6.015
13.03
25.25






Lot 27 (Sample 1)
5.446
11.41
22.10






Lot 27 (Sample 1)
7.222
14.93
28.99






Lot 27 (Sample 1)
8.747
18.31
32.93






Lot 27 (Sample 1)
7.663
14.96
26.58






Lot 27 (Sample 2)
6.733
13.61
24.70
0.54-42.64
1.96
7.54
19.3


Lot 27 (Sample 2)
7.182
14.12
25.15
0.54-44.65





Lot 27 (Sample 2)
6.920
13.26
22.63
0.54-38.24





Lot 27 (Sample 2)
7.400
14.86
27.82






Lot 27 (Sample 2)
6.857
14.08
27.39






Lot 27 (Sample 2)
8.117
16.58
30.90
















TABLE 42







Number-Weighted Distribution Parameters















Circle






Equivalent






(CE)-



CE Dn10
CE Dn50
CE Dn90
diameter-


Formulation
(μm)
(μm)
(μm)
range (μm)





Lot 27 (Sample 1)
1.10
3.92
 8.91
0.54-49.72


Lot 27 (Sample 1)
1.14
4.06
 9.61
0.54-54.14


Lot 27 (Sample 1)
0.95
4.16
 9.85
0.54-55.04


Lot 27 (Sample 2)
1.08
4.24
10.34
0.54-42.64


Lot 27 (Sample 2)
0.85
3.71
10.52
0.54-44.65


Lot 27 (Sample 2)
0.91
4.07
10.55
0.54-38.24









Example: Particle Size Distribution Characterization of Fulvestrant Pharmaceutical Compositions

Fulvestrant pharmaceutical compositions F005g5, Lot 27, Lot 28, and Lot 45, described elsewhere herein, were prepared by the methods of preparation shown schematically as process 101 of FIG. 15. Samples of each Lot were prepared using different processes as indicated in Tables 43 to 50 to achieve fulvestrant particle sizes and particle size distributions. The preparation processes are referred to with alphanumeric identifiers, such as “Process A1,” “Process A2,” and the like, with each process representing a set of fulvestrant-particle-size-reduction steps, as more fully described elsewhere herein, to achieve final fulvestrant particle size and particle size distributions as shown in the Tables 43 to 50. Test samples were evaluated for particle size both prior to drying via lyophilization, which are indicated as “(100x Suspensions)”, and after lyophilization and reconstitution, which are indicated as “(100x Reconstituted Suspensions)” in the Tables 43 to 50. Samples were analyzed with a Malvern Morphologi G3 apparatus for microscopy image capture and analysis. CE diameters were measured and volume-weighted particle size distribution parameters were determined. The CE diameter ranges of measurement samples are also shown, with the lower range value of 0.54 microns representing the lower limit of detection for the apparatus setup. Samples were analyzed with a Malvern Mastersizer 3000 apparatus for laser diffraction particle size characterization of LD diameters.









TABLE 43







Volume-Weighted Distribution Parameters


(100x Reconstituted Suspensions)

















Circle







Equivalent




CE
CE
CE
(CE)-




Dv10
Dv50
Dv90
diameter-


Formulation
Process
(μm)
(μm)
(μm)
range (μm)





Lot 27
Process
6.606
16.14
36.36
0.54-59.46 



A1







Process
7.031
31.23
84.50
0.54-107.10



A2







Process
6.725
24.83
53.11
0.54-84.16 



A3







Process
6.790
43.74
98.32
0.54-105.94



A4






Lot 28
Process
5.333
17.64
41.18
0.54-53.33 



B1







Process
4.863
12.71
42.29
0.54-75.19 



B2







Process
5.376
15.85
49.64
0.54-75.62 



B3







Process
4.144
25.86
82.19
0.54-107.08



B4






Lot 45
Process
8.904
35.32
66.41
0.54-85.05 



C1







Process
8.135
34.79
56.77
0.54-81.50 



C2
















TABLE 44







Volume-Weighted Distribution Parameters


(100x Reconstituted Suspensions)



















Circle









Equivalent
As-Is
Sonicated




















CE
CE
CE
(CE)-
LD
LD
LD
LD
LD
LD




Dv10
Dv50
Dv90
diameter-
Dv10
Dv50
Dv90
Dv10
Dv50
Dv90


Formulation
Process
(μm)
(μm)
(μm)
range (μm)
(μm)
(μm)
(μm)
(μm)
(μm)
(μm)





















Lot 45
Process
5.140
14.44
42.62
0.54-71.31
3.42
8.21
33.8
2.81
5.57
10.6



C9












Lot 45
Process
6.558
17.10
44.70
0.54-74.57
3.37
7.81
32.6
2.82
5.58
10.5



C9












Lot 45
Process
6.648
19.97
56.47
 0.54-112.57
3.50
9.34
43.1
2.81
5.57
10.5



C9












Lot 45
Process
6.541
15.68
37.75
0.54-55.93
3.20
7.08
24.3
2.80
5.52
10.7



C10












Lot 45
Process
5.787
13.11
32.25
0.54-55.82
3.33
7.83
33.9
2.98
5.80
11.1



C10












Lot 45
Process
5.375
14.59
55.02
0.54-88.17
3.38
8.02
35.6
2.97
5.79
11.1



C10












F005g5
As




3.07
29.2
95.1
2.20
5.25
14.0



shown













in













Table













34
















TABLE 45







Volume-Weighted Distribution Parameters


(100x Reconstituted Suspensions)

















Circle







Equivalent




CE
CE
CE
(CE)-




Dv10
Dv50
Dv90
diameter-


Formulation
Process
(μm)
(μm)
(μm)
range (μm)















Lot 27
Process A2
4.547
11.10
33.19
0.54-55.75


Lot 27
Process A2
4.290
10.15
23.66
0.54-49.72


Lot 27
Process A2
5.908
12.98
25.55
0.54-42.63


Lot 27
Process A2
6.075
12.81
23.11
0.54-47.71


Lot 27
Process A2
7.022
15.59
30.94
0.54-69.41


Lot 27
Process A2
5.399
12.22
34.36
0.54-51.56


Lot 27
Process A13
4.89
11.84
32.47



Lot 27
Process A13
6.46
15.33
32.47



Lot 27
Process A13
4.93
11.90
31.23



Lot 27
Process A13
5.54
14.17
50.26



Lot 27
Process A13
4.19
10.16
32.22



Lot 27
Process A13
5.91
13.71
33.81



Lot 27
Process A13
5.10
13.26
45.32



Lot 27
Process A13
4.61
11.47
39.79



Lot 27
Process A13
4.79
12.50
46.19



Lot 27
Process A13
4.71
10.33
22.64



Lot 27
Process A13
5.66
12.66
29.72



Lot 27
Process A13
4.96
11.62
37.81



Lot 27
Process A13
4.22
12.46
42.59



Lot 27
Process A13
5.80
19.69
57.80



Lot 27
Process A13
5.12
11.53
28.37



Lot 27
Process A13
3.84
9.28
32.42



Lot 27
Process A13
4.64
10.32
25.28



Lot 27
Process A13
4.86
11.69
32.44
















TABLE 46







Volume-Weighted Distribution Parameters


(100 × Reconstituted Suspensions)












As-Is
Sonicated
















LD
LD
LD
LD
LD
LD




Dv10
Dv50
Dv90
Dv10
Dv50
Dv90


Formulation
Process
(μm)
(μm)
(μm)
(μm)
(μm)
(μm)





Lot 27
Process
2.03
 8.41
36.0
1.20
3.93
7.97



A13








Lot 27
Process
1.96
 7.83
35.0
1.14
3.69
7.57



A13








Lot 27
Process
2.08
 9.14
41.3
1.20
3.92
7.94



A13








Lot 27
Process
2.10
 9.65
40.3
1.15
3.66
7.53



A13








Lot 27
Process
1.67
 6.10
26.5
1.08
3.42
7.19



A13








Lot 27
Process
1.70
 5.71
21.6
1.17
3.80
7.78



A13








Lot 27
Process
2.53
15.8 
48.4
1.27
4.07
8.72



A13








Lot 27
Process
2.01
12.6 
57.6
1.01
3.04
6.85



A13








Lot 27
Process
1.62
 6.34
29.5
0.96
2.76
5.89



A13
















TABLE 47







Volume-Weighted Distribution Parameters


(100x Suspensions)

















Circle







Equivalent




CE
CE
CE
(CE)-




Dv10
Dv50
Dv90
diameter-


Formulation
Process
(μm)
(μm)
(μm)
range (μm)















Lot 27
Process A15
5.199
10.4
17.52
0.54-27.89



Process A16
3.766
7.411
12.15
0.54-25.43



Process A17
3.053
6.256
10.81
0.54-38.27



Process A18
3.727
7.277
13.91
0.54-31.30


Lot 28
Process B5
4.442
8.585
15.04
0.54-41.23



Process B6
4.134
7.773
13.25
0.54-22.59



Process B7
3.835
7.311
13.11
0.54-25.94



Process B8
3.417
6.644
11.62
0.54-28.25


Lot 45
Process C3
7.160
14.79
25.70
0.54-47.55



Process C4
8.587
18.15
36.68
0.54-62.10
















TABLE 48







Volume-Weighted Distribution Parameters


(100 × Suspensions)












As-Is
Sonicated
















LD
LD
LD
LD
LD
LD




Dv10
Dv50
Dv90
Dv10
Dv50
Dv90


Formulation
Process
(μm)
(μm)
(μm)
(μm)
(μm)
(μm)





Lot 27
Process
1.08
3.29
 7.68
0.91
2.62
6.98



A15









Process
1.03
3.15
 7.00
0.83
2.32
5.72



A16









Process
0.97
2.96
 6.52
0.78
2.13
5.01



A17









Process
0.92
2.91
 6.32
0.72
1.96
4.38



A18








Lot 45
Process C3
1.50
6.03
12.0 
0.83
2.30
5.69



Process C4
1.59
5.82
11.0 
0.85
2.37
5.74
















TABLE 49







Volume-Weighted Distribution Parameters


(100x Suspensions)



















Circle









Equivalent
As-Is
Sonicated




















CE
CE
CE
(CE)-
LD
LD
LD
LD
LD
LD




Dv10
Dv50
Dv90
diameter-
Dv10
Dv50
Dv90
Dv10
Dv50
Dv90


Formulation
Process
(μm)
(μm)
(μm)
range (μm)
(μm)
(μm)
(μm)
(μm)
(μm)
(μm)





















Lot 45
Process
12.320
29.88
57.24
0.54-90.58
1.51
5.40
10.7
0.80
2.11
4.64



C3












Lot 45
Process
7.454
17.37
40.29
0.54-76.61
1.71
6.36
12.5
0.82
2.26
5.20



C4












Lot 45
Process
12.130
27.59
50.08
0.54-87.69
1.73
6.38
12.7
0.79
2.15
4.77



C5












Lot 45
Process
8.193
17.89
35.05
0.54-54.50
1.63
5.85
11.7
0.79
2.13
4.68



C5












Lot 45
Process
8.690
19.36
35.53
0.54-64.77
1.70
6.12
12.0
0.77
2.05
4.45



C5












Lot 45
Process
8.218
17.00
46.80
0.54-80.21
1.46
4.92
9.59
1.36
4.71
9.55



C6












Lot 45
Process
6.455
14.94
38.47
0.54-65.55
1.27
4.21
8.61
0.77
2.11
4.66



C7












Lot 45
Process
7.795
17.20
31.60
0.54-45.03
1.55
5.37
10.7
0.77
2.14
4.81



C8












Lot 45
Process
9.257
20.16
39.47
0.54-84.26
1.64
5.64
11.2
0.78
2.19
4.99



C8












Lot 45
Process
10.050
21.35
36.43
0.54-59.43
1.59
5.55
11.1
0.76
2.10
4.66



C8
















TABLE 50







Volume-Weighted Distribution Parameters


(100 × Suspensions)




















Circle










Equivalent
As-Is
As-Is
As-Is




CE
CE
CE
(CE)-
LD
LD
LD




Dv10
Dv50
Dv90
diameter-
Dv10
Dv50
Dv90


Formulation
Process
(μm)
(μm)
(μm)
range (μm)
(μm)
(μm)
(μm)





Lot 27
Process A5 
5.506
12.94
26.24
0.54-52.71
1.54
5.70
11.3 


Lot 27
Process A6 
8.740
19.30
35.62
0.54-54.43
1.42
5.10
10.1 


Lot 27
Process A7 
7.862
18.92
36.09
0.54-52.63
1.48
5.30
10.4 


Lot 27
Process A8 
8.184
17.49
33.02
0.54-63.56
1.46
5.04
 9.69


Lot 27
Process A9 
7.451
15.99
29.94
0.54-55.58
1.49
5.00
 9.65


Lot 27
Process A10
7.673
18.50
36.71
0.54-74.22
1.59
5.55
10.6 


Lot 27
Process A11
9.093
20.01
45.26
0.54-61.26
1.72
6.11
12.1 


Lot 27
Process A12
6.355
14.92
46.31
0.54-63.98
1.66
5.77
10.9 


Lot 27
Process A13
7.029
15.66
31.06
0.54-55.89
1.07
3.51
 7.32


Lot 27
Process A14
7.870
20.15
43.79
0.54-62.35
1.74
5.87
11.0 


Lot 27
Process A14
8.499
19.06
37.90
0.54-70.88
1.67
5.49
10.5 


Lot 27
Process A14
8.072
17.43
30.90
0.54-56.50
1.76
6.01
11.5 


Lot 27
Process A14
8.078
18.98
45.32
0.54-69.82
1.81
6.43
12.5 









When ranges are used herein for chemical or physical properties, such as particle size or particle size distribution, formulation component concentrations, or pharmacokinetic properties, all combinations, and subcombinations of ranges for specific embodiments therein are intended to be included.


The disclosures of each patent, patent application, and publication cited or described in this document are hereby incorporated herein by reference, in its entirety.


Those skilled in the art will appreciate that numerous changes and modifications can be made to the preferred embodiments of the invention and that such changes and modifications can be made without departing from the spirit of the invention. It is, therefore, intended that the appended claims cover all such equivalent variations as fall within the true spirit and scope of the invention.

Claims
  • 1. A method of forming an aqueous fulvestrant suspension comprising: mixing an aqueous medium and at least one stabilizer to form a suspension vehicle, the at least one stabilizer comprising one surfactant and a polyvinylpyrrolidone, polyethylene glycol 3350, or a carboxymethylcellulose sodium, or one surfactant and one non-electrolyte;adding an amount of fulvestrant to the suspension vehicle; anddispersing the fulvestrant in the suspension vehicle to form the aqueous fulvestrant suspension.
  • 2. An aqueous fulvestrant suspension prepared according to the method of claim 1.
  • 3. A pharmaceutical composition comprising the aqueous fulvestrant suspension of claim 2, wherein optionally the pharmaceutical composition comprises fulvestrant particles: having one or more of: a laser diffraction determined (LD) Dv(10) between about 1 micron to about 3 microns;an LD Dv(50) between about 2 microns and about 35 microns; andan LD Dv(90) between about 4 microns and about 120 microns;and having one or more of: an LD Dv(10) between about 1-2 microns;an LD Dv(90) between about 6-9 microns; andan LD Dv(50) between about 2-4 microns;and having one or more of: a microscopy image capture determined (CE) Dv(90) between about 10 microns and about 200 microns;a CE Dv(50) between about 5 microns and about 60 microns; anda CE Dv(10) between about 1 microns and about 25 microns;and having a CE Dv(90) between about 10 microns and about 200 microns;a CE Dv(50) between about 5 microns and about 60 microns; ora CE Dv(10) between about 1 microns and about 25 microns.
  • 4. The method of claim 1, further comprising homogenizing the aqueous fulvestrant suspension.
  • 5. The method of claim 4, wherein the high pressure homogenization is performed at a pressure of about 15,000 psi to about 45,000 psi.
  • 6. The method of claim 4, further comprising adding an electrolyte to the homogenized aqueous fulvestrant suspension and mixing the electrolyte into the suspension.
  • 7. The method of claim 4, further comprising adding a non-electrolyte to the homogenized aqueous fulvestrant suspension and mixing the non-electrolyte into the suspension.
  • 8. The method of claim 1, further comprising concentrating the fulvestrant suspension by phase separating the suspension and removing a portion of the supernatant.
  • 9. The method of claim 1, further comprising drying the aqueous suspension to form a dried pharmaceutical composition.
  • 10. The method of claim 9, further comprising sterilizing the dried pharmaceutical composition using gamma irradiation.
  • 11. The method of claim 10, further comprising reconstituting the dried pharmaceutical composition into a second aqueous suspension by adding at least one of water for injection (WFI), normal saline, and 5% dextrose in water.
CROSS REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. application Ser. No. 16/099,265, filed Nov. 6, 2018 which is a National Stage Application filed under 35 U.S.C. 371 of International Application No. PCT/US2017/031376 filed May 5, 2017 which claims the benefit of U.S. Provisional Application No. 62/332,842, filed May 6, 2016, and U.S. Provisional Application No. 62/420,555, filed Nov. 10, 2016, the entireties of which are incorporated by reference herein.

Provisional Applications (2)
Number Date Country
62420555 Nov 2016 US
62332842 May 2016 US
Continuations (1)
Number Date Country
Parent 16099265 Nov 2018 US
Child 17379534 US