EP1221942A1 - Microparticules biodegradables contenant une nouvelle proteine stimulant l'erythropoietine - Google Patents

Microparticules biodegradables contenant une nouvelle proteine stimulant l'erythropoietine

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Publication number
EP1221942A1
EP1221942A1 EP00973798A EP00973798A EP1221942A1 EP 1221942 A1 EP1221942 A1 EP 1221942A1 EP 00973798 A EP00973798 A EP 00973798A EP 00973798 A EP00973798 A EP 00973798A EP 1221942 A1 EP1221942 A1 EP 1221942A1
Authority
EP
European Patent Office
Prior art keywords
nesp
microparticles
active ingredient
polymer
protein
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP00973798A
Other languages
German (de)
English (en)
Inventor
Paul Burke
Lisa Klumb
Keith Murphy
John Herberger
Donna L. French
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Amgen Inc
Original Assignee
Amgen Inc
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Filing date
Publication date
Application filed by Amgen Inc filed Critical Amgen Inc
Priority claimed from PCT/US2000/029257 external-priority patent/WO2001030320A1/fr
Publication of EP1221942A1 publication Critical patent/EP1221942A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction

Definitions

  • the present invention relates to a composition for the sustained release of biologically active, novel erythropoietin stimulating protein (NESP) , and improved methods of forming said composition.
  • the composition comprises polymeric microparticles within which particles of NESP have been dispersed.
  • the improved method utilizes a cosolvent mixture to effect more efficient and rapid removal of residual polymer solvents during any drying process.
  • sustained-release formulations which could provide a means of controlling blood levels of the active ingredient, and also provide greater efficacy, safety, patient convenience and patient compliance.
  • instability of most proteins e.g. denaturation and loss of bioactivity upon exposure to heat, organic solvents, etc.
  • sustained-release formulations have greatly limited the development and evaluation of sustained-release formulations .
  • the major disadvantages associated with the above-referenced methods may include, under certain circumstances: 1) high temperatures causing protein inactivation; 2) exposure to organic solvents causing protein inactivation; 3) inability to encapsulate hydrophilic drugs due to loss of drug to the aqueous phase which is used to extract the organic solvent; 4) the large amount of organic solvents normally needed during the processes, and which cannot be adequately removed from the final product, i.e., high residual solvent levels in final product; 5) poor protein loading efficiencies; 6) poor overall yields; 7) problems with drug leakage and/or high initial drug release upon administration; and 8) expensive and complex to scale- up.
  • Erythropoietin is a glycoprotein hormone involved in the maturation of erythroid progenitor cells into erythrocytes . It is produced in the kidney and is essential in regulating levels of red blood cells in the circulation. Conditions marked by low levels of tissue oxygen signal increased production of erythropoietin, which in turn stimulates erythropoiesis . A loss of kidney function as is seen in chronic renal failure (CRF) , for example, typically results in decreased production of erythropoietin and a concomitant reduction in red blood cells .
  • CRF chronic renal failure
  • rHuEPO recombinant human erythropoietin
  • rHuEPO is administered every day 10 days prior to surgery, on the day of surgery, and four days thereafter (EPOGEN ® Package Insert, 12/23/96) .
  • the current recommended starting doses for rHuEPO raise hematocrit into the target range in about six to eight weeks.
  • a maintenance dosing schedule is established which will vary depending upon the patient, but is typically three times per week for anemic patients with CRF.
  • the administration of rHuEPO described above is an effective and well-tolerated regimen for the treatment of anemia.
  • Zale et al . U.S. Patent No.
  • compositions of non-aggregated, biologically active EPO comprise a polymeric matrix of a biocompatible polymer and particles of biologically active, aggregation- stabilized EPO, wherein said particles are dispersed within the biocompatible polymer, and wherein said microparticles are prepared using the process described in U.S. Patent No. 5,019,400.
  • the method described and claimed utilizes a salting-out excipient to stabilize the EPO.
  • the formulation is said to have advantages including longer, more consistent in vivo blood levels of EPO, lower initial bursts of EPO, and increased therapeutic benefits by eliminating fluctuations in serum EPO levels.
  • Recombinant human erythropoietin expressed in mammalian cells contains three N-linked and one 0-linked oligosaccharide chains which together comprise about 40% of the total molecular weight of the glycoprotein.
  • N-linked glycosylation occurs at asparagine residues located at positions 24, 38 and 83 while O-linked glycosylation occurs at a serine residue located at position 126; Lai et al . , J. Biol . Chera . , 261 : 3116 (1986); Broudy et al . , Arch . Biochem . Biophys . , 2.65:329 (1988).
  • the oligosaccharide chains have been shown to be modified with terminal sialic acid residues.
  • Enzymatic treatment of glycosylated erythropoietin to remove sialic acid residues results in a loss of in vivo activity but does not affect in vi tro activity; Lowy et al., Nature, 185:102 (1960); Goldwasser et al.,
  • Novel erythropoietin stimulating protein is a hyperglycosylated erythropoietin analog having five changes in the amino acid sequence of rHuEPO which provide for two additional carbohydrate chains. More specifically, NESP contains two additional N-linked carbohydrate chains at amino acid residues 30 and 88 (numbering corresponding to the sequence of human EPO) (see PCT Application No. US94/02957, herein incorporated by reference in its entirety) . NESP is biochemically distinct from EPO, having a longer serum half-life and higher in vivo biological activity; Egrie et al., ASH 97, Blood, 90:56a (1997).
  • NESP has been shown to have ⁇ 3 fold increase in serum half-life in mice, rats, dogs and man; Id.
  • mice the longer serum half-life and higher in vivo activity allow for less frequent dosing (once weekly or once every other week) compared to rHuEPO to obtain the same biological response; Id.
  • NESP has a significantly longer serum half-life than rHuEPO in chronic renal failure patients, suggesting that a less frequent dosing schedule may also be employed in humans; MacDougall, et al . , J American Society of Nephrology, 8:268A (1997) .
  • a less frequent dosing schedule would be more convenient to both physicians and patients, and would be particularly helpful to those patients involved in self-administration.
  • Other advantages to less frequent dosing may include less drug being introduced into patients, a reduction in the nature or severity of the few side-effects seen with rHuEPO administration, and increased compliance.
  • the present invention is based upon the discovery that NESP can be encapsulated in microparticles and provide a pharmaceutical composition with an even more dramatic sustained release profile, allowing for a once every 4-6 week dosing for raising hematocrit and treating anemia, and thus providing tremendous therapeutic advantage. Additionally, the NESP/PLGA system is such that the PLGA component is cleared (biodegraded) up to at least one week prior to the cessation of therapeutic effect, and thus allow for repeated dosing with less concern of polymer and drug build-up from dose to dose. Such a system may not be possible with, for example, EPO/PLGA microparticles.
  • the present invention provides an improved, economical, scalable method for microparticle preparation which is broadly applicable to biologically active agents other than NESP, including peptides and small molecules.
  • one aspect of the present invention is a pharmaceutical composition for the sustained-release of an active ingredient comprising a biologically active ingredient contained within polymeric microparticles.
  • the sustained- release compositions of the present invention maintain the activity, integrity and safety of the active ingredient during encapsulation and release, which helps to provide for longer periods of consistent release.
  • a second aspect of the present invention relates to a new and improved process for preparing a sustained-release composition comprising an active ingredient contained within polymeric microparticles.
  • the process is economical, amenable to aseptic processing, scalable and broadly applicable to proteins, peptides, and small molecules.
  • the improved process can be generally described as comprising the steps of: (a) obtaining a dried powder of a specific active ingredient or formulated active ingredient; (b) preparing a polymer solution comprising a polymer dissolved in a cosolvent mixture; (c) dispersing said dried powder in said polymer solution to produce an active ingredient/polymer mixture; (d) preparing active ingredient-containing microparticles from said mixture; (e) collecting said microparticles; and (f) finishing said microparticles by secondary drying.
  • the drying times associated with this process are significantly reduced as compared to prior art methods.
  • Figure 1 is a schematic of the process of the present invention for making the active ingredient containing microparticles.
  • Figure 2 shows chromatograms depicting the size exclusion chromatography results for a NESP preparation prior to spray drying ( . . . ) , a spray dried NESP protein powder ( ) , and a typical result for NESP after microparticle encapsulation ( ) .
  • Figure 3 is a graph depicting NESP serum levels for various microparticle preparations which had been injected subcutaneously (360 ⁇ g/kg NESP peptide dose) into rats. Serum concentration is plotted vs. time (days) .
  • Figure 4 is a graph depicting hematocrit for rats injected subcutaneously (360 ⁇ g/kg NESP peptide dose) with various microparticle preparations. Hematocrit (%) is plotted vs. time (days) .
  • Figure 5 is a graph depicting NESP serum levels for various microparticle preparations which had been injected subcutaneously (360 ⁇ g/kg NESP peptide dose) into rats. Serum concentration is plotted vs. time (days) .
  • Figure 6 is a graph depicting NESP serum levels for various microparticle preparations which had been injected subcutaneously (360 ⁇ g/kg NESP peptide dose) into rats. Serum concentration is plotted vs. time (days) .
  • Figure 7 is a graph depicting hemoglobin levels for rats injected subcutaneously with a 10,000 ⁇ g/kg bolus injection of NESP vs. a 100 ⁇ g/kg (20 mg microparticle) injection of a NESP microparticle preparation (50:50, inherent viscosity 0.4 dL/g) . Hemoglobin levels (g/dL) is plotted vs. time (days) .
  • Figure 8 is a graph depicting NESP serum levels for various microparticle preparations which had been injected subcutaneously (360 ⁇ g/kg NESP peptide dose) into rats. Serum concentration is plotted vs. time (days) .
  • Figure 9 is a graph depicting leptin serum levels for rats injected with various leptin preparations. Serum concentration is plotted vs. time (hours) .
  • Figure 10 is a graph depicting % weight loss for rats injected with various leptin preparations. Body weight (mg) is plotted vs. time (days) .
  • Figure 11 is a graph depicting NESP serum levels for microparticle preparations which had been injected subcutaneously (360 ⁇ g/kg NESP peptide dose) into rats. Serum concentration is plotted vs. time (days) .
  • Figure 12 is a graph depicting hematocrit for rats injected subcutaneously (360 ⁇ g/kg NESP peptide dose) with microparticle preparations. Hematocrit (%) is plotted vs. time (days) .
  • Figure 13 is a graph depicting NESP serum levels for microparticle preparations which had been injected subcutaneously (360 ⁇ g/kg NESP peptide dose) into rats. Serum concentration is plotted vs. time (days) .
  • Figure 14 is a graph depicting hematocrit for rats injected subcutaneously (360 ⁇ g/kg NESP peptide dose) with microparticle preparations. Hematocrit (%) is plotted vs. time (days) .
  • microparticles can be used to encompass microparticles, microspheres, and microcapsules .
  • the present invention provides a pharmaceutical composition for the sustained-release of an active ingredient comprising a biologically active ingredient contained within polymeric microparticles.
  • a sustained-release composition is defined as a release of biologically active agent which results in measurable serum levels of said agent for a period of time longer than that obtained following direct administration of aqueous biologically active agent.
  • the sustained release can be continuous or discontinuous, linear or non-linear, and this can be accomplished using one or more polymer compositions, drug loadings, selection of excipients, or other modifications.
  • the sustained-release composition will comprise the biologically active ingredient, NESP.
  • NESP of the present invention is a hyperglycosylated EPO analog comprising two additional glycosylation sites with an additional carbohydrate chain attached to each site.
  • NESP was constructed using site-directed mutagenesis and expressed in mammalian host cells. Details of the production of NESP are provided in co-owned PCT Application No. US94/ 02957. New N-linked glycosylation sites for rHuEPO were introduced by alterations in the DNA sequence to encode the amino acids Asn-X-Ser/Thr in the polypeptide chain. DNA encoding NESP was transfected into Chinese Hamster Ovary (CHO) host cells and the expressed polypeptide was analyzed for the presence of additional carbohydrate chains.
  • NESP will have two additional N-linked carbohydrate chains at residues 30 and 88.
  • the numbering of the amino acid sequence is that of human erythropoietin (EPO) .
  • the amino acid sequence of EPO is that depicted in SEQ ID NO: 1.
  • the amino acid sequence of NESP is that depicted in SEQ ID NO: 2. It is understood that NESP will have the normal complement of N-linked and O-linked glycosylation sites in addition to the new sites.
  • the NESP of the present invention may also include conservative amino acid changes at one or more residues in SEQ ID NO: 2. These changes do not result in addition of a carbohydrate chain and will have little effect on the biological activity of the analog.
  • active ingredients to be incorporated into the microparticles of the present invention are synthetic or natural compounds which demonstrate a biological effect when introduced into a living creature.
  • Contemplated active agents include peptides, small molecules, carbohydrates, nucleic acids, lipids, proteins, and analogs thereof.
  • Proteins contemplated for use include potent cytokines, including various hematopoietic factors such as G-CSF, GM-CSF, M-CSF, MGDF, the interferons (alpha, beta, and gamma) , interferon consensus, the interleukins (1-12), erythropoietin (EPO) , fibroblast growth factor, KGF, TNF, TNFbp, IL-lra, stem cell factor, nerve growth factor, GDNF, BDNF, NT3 , platelet-derived growth factor, and tumor growth factor (alpha, beta) , osteoprotegerin (OPG) , NESP, and OB protein.
  • OB protein will also be referred to as leptin.
  • compositions of the present invention are derivatives, fusion proteins, conjugates, analogs or modified forms of the natural active ingredients.
  • Chemical modification of biologically active proteins has been found to provide additional advantages under certain circumstances, such as increasing the stability and circulation time of the therapeutic protein and decreasing immunogenicity .
  • Davis et al . U.S. Patent No. 4,179,337, discloses conjugation of water-soluble polypeptides such as enzymes and insulin to polyethylene glycol (PEG); see also Kinstler et al., U.S. Patent No. 5,824,784.
  • compositions comprising effective amounts of protein or derivative products of the invention together with pharmaceutically acceptable diluents, stabilizers, preservatives, solubilizers, emulsifiers, adjuvants and/or carriers.
  • compositions include diluents of various buffer content (e.g., Tris-HCl, phosphate), pH and ionic strength; additives such as detergents and solubilizing agents (e.g., Polysorbate 20, Polysorbate 80), anti-oxidants (e.g., ascorbic acid, sodium metabisulfite) , preservatives (e.g., Thimerosol, benzyl alcohol) and bulking substances (e.g., lactose, mannitol); see, e . g. , Remington's Pharmaceutical Sciences, 18th Ed. (1990, Mack Publishing Co., Easton, PA 18042) pages 1435-1712 which are herein incorporated by reference.
  • An effective amount of active ingredient is a therapeutically, prophylactically, or diagnostically effective amount, which can be readily determined by a person skilled in the art by taking into consideration such factors as body weight, age, therapeutic or prophylactic or diagnostic goal, and release rate desired.
  • the term "therapeutically effective amount” refers to an amount which gives an increase in hematocrit that provides benefit to a patient. The amount will vary from one individual to another and will depend upon a number of factors, including the overall physical condition of the patient and the underlying cause of anemia. For example, a therapeutically effective amount of rHuEPO for a patient suffering from chronic renal failure is 50 to 150 units/kg three times per week. The amount of rHuEPO used for therapy gives an acceptable rate of hematocrit increase and maintains the hematocrit at a beneficial level (usually at least about 30% and typically in a range of 30% to 36%) .
  • a therapeutically effective amount of the present compositions may be readily ascertained by one skilled in the art using publicly available materials and procedures.
  • the invention provides for administering NESP- containing microparticles less frequently than NESP and/or EPO.
  • the dosing frequency will vary depending upon the condition being treated, but in general will be about one time per 4-6 weeks. It is understood that the dosing frequencies actually used may vary somewhat from the frequencies disclosed herein due to variations in responses by different individuals to the NESP- containing microparticles; the term "about” is intended to reflect such variations .
  • the present invention may thus be used to stimulate red blood cell production and correct depressed red cell levels. Most commonly, red cell levels are decreased due to anemia.
  • the conditions treatable by the present invention include anemia associated with a decline or loss of kidney function (chronic renal failure) , anemia associated with myelosuppressive therapy, such as chemotherapeutic or anti-viral drugs (such as AZT), anemia associated with the progression of non-myeloid cancers, and anemia associated with viral infections (such as HIV) .
  • myelosuppressive therapy such as chemotherapeutic or anti-viral drugs (such as AZT)
  • anemia associated with the progression of non-myeloid cancers such as HIV
  • HIV viral infections
  • any condition treatable with rHuEPO may also be treated with the NESP- containing microparticles of the invention.
  • the invention also provides for administration of a therapeutically effective amount of iron in order to maintain increased erythropoiesis during therapy.
  • the amount to be given may be readily determined by one skilled in the art based upon therapy with rHuEPO.
  • the present invention also provides an improved method for preparing polymeric microparticles containing an active ingredient, comprising utilization of a cosolvent mixture to effect more rapid removal of organic solvents during drying.
  • the residual presence of secondary organic solvent components in the mixture during drying results in acceleration of the removal of residual polymer solvent during any drying process.
  • This improved method provides several significant advantages over the processes described in the art, including, for example, 1) reduction of levels of residual solvents in the polymer system after the initial microparticle formation step; 2) reduction in drying cycle times for polymer systems; and 3) enabling the removal of toxic solvents to acceptable levels for use in human pharmaceuticals. Importantly, these advantages help make such processes commercially practical .
  • the principal embodiment of the improved method for making the protein loaded microparticles comprises: (a) obtaining a dried powder of an active ingredient or formulated active ingredient, (b) dissolving a polymer in a cosolvent mixture to produce a polymeric solution; (c) adding said dried powder to said polymeric solution to produce a active ingredient/polymer mixture; (d) spray drying said mixture to produce the desired active ingredient loaded microparticles; (e) collecting said microparticles; and (f) finishing said microparticles by secondary drying.
  • the process is shown schematically in Figure 1.
  • the active ingredient or formulated active ingredient will be in the form of a spray dried powder.
  • Spray drying is a process wherein a solution is atomized to form a fine mist and dried by direct contact with hot carrier gases.
  • spray drying see e . g. , Masters, K. , "Spray Drying Handbook" (John Wiley & Sons, eds . , New York 1984).
  • an improved commercial scale spray dried protein powder preparation method which results in significantly higher yields and improved collection of the microparticles.
  • Polymer solvents contemplated for use in step b) of the present processes include, for example, chloroform, ethyl acetate, acetone, methylene chloride, and dimethylsulfoxide .
  • the polymer solvent to be used is methylene chloride.
  • Non-solvents contemplated for use include ethanol, ethyl formate, and heptane.
  • the microparticle preparation step (d) may alternatively involve an emulsion based preparation, or spray freezing.
  • the organic : aqueous ratios contemplated for use are 1:1 to 12:1.
  • the microparticles prepared by the methods of the present invention will generally comprise 0.001-60% by weight of protein.
  • Secondary drying processes contemplated for use in step (f) include gas bleed drying, fluidized bed drying, lyophilization, vacuum drying, and tray drying.
  • gas bleed drying is utilized in step (f ) .
  • Biodegradable means that the composition will erode or degrade in vivo to form smaller biocompatible chemical species. Degradation may occur, for example, by enzymatic, chemical or physical processes.
  • Suitable biodegradable polymers contemplated for use in the present invention include poly (lactide) s, poly (glycolide) s, poly (lactic acid)s, poly (glycolic acid)s, polyanhydrides, polyorthoesters, polyetheresters, polycaprolactone, polyesteramides, polyphosphazenes, polyphosphoesters, pseudo-polyamino acids; Langer, Nature, 292:5-10 (1998), blends and copolymers thereof.
  • the range of molecular weights contemplated for the polymers to be used in the present processes can be readily determined by a person skilled in the art based upon such factors the desired polymer degradation rate. Typically, the range of molecular weight will be 2000 to 2,000,000 Daltons. Almost any type of polymer can be used provided the appropriate solvent or cosolvent system are found.
  • the term "PLGA" as used herein is intended to refer to a polymer of lactic acid alone, a polymer of glycolic acid alone, a mixture of such polymers, a copolymer of glycolic acid and lactic acid, a mixture of such copolymers, or a mixture of such polymers and copolymers. PLGA's used may be in the free acid
  • the biodegradable polymer will be poly lactide-co-glycolide (PLGA) .
  • the polymer concentrations contemplated for use in the processes of the present invention are in the range of 5-70 g/lOOmL
  • an aqueous solution, a suspension, or a solid form of the active agent can be admixed with the organic solvent containing the polymer.
  • an aqueous solution of active ingredient is used, an aqueous solution of active ingredient-in-polymer solution emulsion, or a water-in-oil emulsion is formed (containing the active ingredient in the aqueous phase and the polymer in the organic phase) and used to prepare microparticles.
  • a suspension or solid form of active ingredient suspensions of the solid active ingredient in the polymer solution are formed and used to prepare the microparticles.
  • a monophasic solution of active ingredient and polymer may be used.
  • the active ingredient will be in the form of a spray dried powder
  • the particle size of the protein powder will be in the range of ⁇ 10 ⁇ m.
  • the protein concentrations contemplated for use in the processes of the present invention are in the range of 0.001-500 mg/mL when in the emulsion or suspension.
  • the active ingredient solution, suspension, emulsion, or solid form may also be formulated, i.e., include a buffer, a surfactant, or an excipient which serves to stabilize the active ingredient during drying, e.g., trehalose, ammonium sulfate, 2-hydroxy propyl ⁇ - cyclodextrin, sucrose, or other protein-stabilizing sugars or excipients.
  • a buffer e.g., trehalose, ammonium sulfate, 2-hydroxy propyl ⁇ - cyclodextrin, sucrose, or other protein-stabilizing sugars or excipients.
  • a suspension of protein loaded microparticles prepared in accordance with the present invention is preferably administered by injection intraperitoneally, subcutaneously, or intramuscularly.
  • routes of delivery could also be effectively utilized using the compositions of the present invention.
  • Example 1 describes a method for preparing protein loaded microparticles using spray drying for the microparticle preparation.
  • NESP in the form of a spray dried protein powder
  • Example 2 describes various characterization experiments performed on the NESP-containing microparticles of Example 1.
  • Example 3 demonstrates the ability of NESP-containing microparticles of Example 1 to provide for sustained release of NESP in vivo .
  • Example 4 describes a novel method for preparing polymeric microparticles wherein a cosolvent is utilized to effect more rapid and effective removal of residual solvent.
  • Example 5 describes a method for preparing NESP-containing microparticles using spray freezing for the microparticle preparation step.
  • Example 6 describes various characterization experiments performed on the NESP-containing microparticles of Example 5.
  • Example 7 demonstrates the ability of NESP-containing microparticles of Example 5 to provide for sustained release of NESP in vivo .
  • Example 8 describes the double emulsion/solvent extraction and evaporation method for preparing PLGA microparticles containing NESP, and demonstrates the ability to provide for sustained release of NESP in vivo .
  • Example 9 describes the preparation of leptin- containing microparticles using the process of Example 1 and demonstrates the ability of the leptin-containing microparticles to provide for sustained release of leptin in vivo .
  • Example 10 describes a method for preparing protein loaded microparticles using spray drying for the microparticle preparation.
  • Example 11 describes various characterization experiments performed on the NESP-containing microparticles of Example 10.
  • Example 12 demonstrates the ability of NESP-containing microparticles of Example 10 to provide for sustained release of NESP in vivo .
  • Example 13 demonstrates the ability of NESP-containing microparticles of Example 10 to provide for sustained release of NESP in vivo .
  • This example describes a method for preparing protein loaded microparticles; specifically, the preparation of poly (D, L-lactide-co-glycolide) microspheres containing NESP, using spray drying for the microparticle preparation step.
  • NESP was formulated at 46% NESP, 29% sodium phosphate salts, 25% trehalose (w/w/w) and spray dried on a lab scale spray dryer (BUCHI 190) using the following conditions: feed rate 2.0 ml/min, atomization 500 NL/hour, inlet temperature 135 °C, outlet temperature 99°C, drying gas flow rate 800 SLPM.
  • feed rate 2.0 ml/min feed rate 2.0 ml/min
  • atomization 500 NL/hour inlet temperature 135 °C
  • outlet temperature 99°C outlet temperature 99°C
  • drying gas flow rate 800 SLPM drying gas flow rate
  • the protein powder was added to a PLGA in dichloromethane (inherent viscosity 0.18, 11 kD) polymer solution (40% w/v) and the resulting suspension was spray dried on a pilot plant scale spray dryer (Niro Mobile MinorTM) using the following conditions: feed rate 50 ml/min, atomization flow rate (two-fluid nozzle) 3.0 kg/hr, inlet gas temperature 50°C, outlet temperature 30°C, drying gas flow rate 93 kg/hr.
  • the resulting NESP-containing microparticles (0.53% NESP) were then collected and characterized after sieving (125 ⁇ m mesh size) .
  • NESP-containing microparticles of various PLGA composition were produced using this process.
  • the PLGA compositions differed in the copolymer ratio of lactide:glycolide from 50:50 to 100% lactide.
  • the PLGA polymers used had free acid polymer chain end groups.
  • This example describes various characterization experiments performed on the spray dried NESP/trehalose protein powder and the NESP- containing microparticles described in Example 1.
  • the NESP/trehalose protein powder was characterized by size exclusion chromatography under native conditions; monomer percent was unchanged post spray drying (>99.8%)(See Figure 2). No additional aggregate were observed by sodium dodecyl polyacrylamide gel electrophoresis (SDS-PAGE) , using silver stain.
  • the protein powder was analyzed by reverse phase high performance liquid chromatography (RP-HPLC) ; no change from the unprocessed NESP was observed.
  • the protein powder was also characterized by an HPLC glycoform assay and isoelectric focusing gel electrophoresis (IEF) and IEF western blot; no change in glycoform distribution was observed.
  • Radioimmunoassay of the reconstituted powder demonstrated full antibody recognition, and tryptic mapping demonstrated no change in oxidation from the unprocessed material.
  • the particle size distribution of the protein powder was determined by Fraunhoffer diffraction to have mean volume distribution of 4.7 ⁇ m.
  • the particle size of the NESP-containing microparticles was 58 ⁇ 8 ⁇ m for the mean of the volume distribution determined by Fraunhoffer diffraction, averaged over the 5 lots .
  • the post-encapsulation integrity of NESP within these microparticles was assessed by extracting the protein and analyzing the extracts via anion exchange and size exclusion HPLC under native conditions.
  • To extract the NESP from the microparticles approximately 20 mg of microparticles were placed in a tube with 1 mL acetonitrile . The samples were vortexed for 10-20 seconds and centrifuged at 14,000 rpm for 2 minutes at 4°C to pellet the protein and excipients .
  • the supernatant was removed and the pellet resuspended in 1 mL acetonitrile. The above steps were performed three more times. After final supernatant removal, samples were dried in a vacuum oven for 2-3 hours at room temperature. The NESP pellet was reconstituted in 20mM sodium phosphate, pH 6.0, with or without 0.005% Tween 80. After gentle flicking of the tube the sample was incubated at room temperature for 2 hours to achieve full dissolution. Protein was quantitated and integrity determined by anion exchange in series with size exclusion HPLC. Protein recovery was quantitative (>99%) and protein integrity was 98.2 ⁇ 1.0% monomeric by size exclusion HPLC averaged over the 5 lots, each lot characterized in triplicate (See Figure 2).
  • the extract from the 75% lactide formulation was additionally characterized by radioimmunoassay, capillary electrophoresis, and peptide mapping.
  • the RIA resulted in protein recoveries consistent with the SEC results, demonstrating antibody recognizable protein.
  • Capillary electrophoresis confirmed that the glycoform distribution was unchanged from the unprocessed NESP.
  • the extent of oxidation as determined from peptide mapping was equivalent to the unprocessed NESP.
  • Example 1 to provide for sustained release of NESP in vivo.
  • NESP-containing microparticles (360 ⁇ g/kg NESP peptide dose) were injected subcutaneously at the nape of the neck of Male Sprague Dawley rats (385 ⁇ 14 g) .
  • a subcutaneous , single injection bolus of NESP in a dose equivalent to the microparticles was included as a control.
  • Blood samples were taken from the tail vein at times post injection up to 8 weeks.
  • the NESP concentration in the rat serum was determined by ELISA through 2 and 4 weeks .
  • Whole blood was analyzed for hematocrit, hemoglobin, and reticulocyte counts.
  • NESP serum levels from a single injection of NESP-containing microparticles fabricated from 50:50 lactide: glycolide polymer were > 1 ng/mL for 15 days for all three lots studied (See Figure 3) .
  • the NESP alone given as a single bolus had elevated serum levels for 11 days (See Figure 3).
  • the NESP-containing microparticles elevated the hemoglobin and hematocrit above baseline for 25 and 28 days, respectively (See Figure 4) .
  • NESP bolus had elevated hemoglobin and hematocrit for 25 days (See Figure 4) .
  • NESP serum levels from a single injection of NESP-containing microparticles fabricated from 75:25 lactide: glycolide polymer were > 1 ng/mL for 20 days
  • the NESP-containing microparticles elevated the hemoglobin and hematocrit above baseline for > 40 days (See Figure 4) .
  • NESP serum levels from a single injection of NESP-containing microparticles fabricated using a solution mixture of 50:50 and 100% lactide polymers to create an overall average 75% lactide polymer were > 1 ng/mL for 18 days (See Figure 3) .
  • the NESP-containing microparticles elevated the hemoglobin and hematocrit above baseline for 35 days (See Figure 4) .
  • This example describes the novel method for preparing microparticles wherein a cosolvent is utilized to effect more rapid and effective removal of residual solvent; specifically, the preparation of poly(D,L- lactide-co-glycolide) microspheres utilizing an ethanol/methylene chloride cosolvent mixture.
  • Two batches of 50:50 PLGA (11 kD) microparticles were produced by spray drying.
  • pure methylene chloride was used to dissolve a mass of PLGA equal to 26% of the solvent mass.
  • a cosolvent of methylene chloride (86. 4% by mass) and ethanol (13.6% by mass) was used to dissolve a mass of PLGA equal to 26% of the cosolvent mass) .
  • the resulting solutions were spray dried on a pilot plant scale spray dryer (Niro Mobile MinorTM) using the following conditions: feed rate 50 ⁇ 5 ml/min, atomization flow rate (two-fluid nozzle) 60 SLPM, inlet gas temperature 55°C, outlet temperature 33-36 °C, drying gas flow rate 2.1 lbs/min.
  • feed rate 50 ⁇ 5 ml/min feed rate 50 ⁇ 5 ml/min
  • atomization flow rate two-fluid nozzle
  • inlet gas temperature 55°C
  • outlet temperature 33-36 °C outlet temperature 33-36 °C
  • the resulting microparticles were collected and characterized.
  • the residual solvent concentration in Batch 1 following spray drying was 18550 ppm methylene chloride.
  • the residual solvent concentrations in Batch 2 following spray drying were 6190 ppm methylene chloride, 3330 ppm ethanol .
  • Secondary drying was performed on both batches as follows: the microparticles were placed in a 1.5" diameter dryer on a retaining screen. The dryer was sealed and nitrogen was flowed through the bed at 4.4 L/min. The dryer was submerged in a heating bath for temperature control. After Batch 1 was dried for 73 hours, starting at 20°C and ending at 41°C, the residual methylene chloride level was 750 ppm. Batch 2 was dried for 40 hours, starting at 18°C and ending at 30°C. These microparticles reached residual solvent levels of 487 ppm methylene chloride and 455 ppm ethanol.
  • This example describes a method for preparing protein loaded microparticles; specifically, the preparation of poly (D, L-lactide-co-glycolide) microspheres containing NESP, using spray freezing for the microparticle preparation step.
  • NESP trehalose formulation from Example 1, and an ammonium sulfate formulation
  • the ammonium sulfate formulation for NESP was: 11% NESP, 10% phosphate salts, 79% ammonium sulfate (w/w/w) .
  • Microparticles containing the NESP/trehalose protein powder were prepared from unblocked PLGA obtained from either Alkermes/Medisorb Wilmington, Ohio, or Boehringer Ingelheim Chemicals, Inc., Montvale, N.J. or blocked PLGA from Boehringer Ingelheim.
  • the polymer inherent viscosities ranged from 0.14 dL/g to 0.5 dL/g (11 - 47 kD molecular weight) , and the lactide contents were from 50% to 100%.
  • NESP/ammonium sulfate protein powder was encapsulated in unblocked PLGA (50:50) with an inherent viscosity of 0.18 dL/g (11 kD) .
  • the method described by Gombotz et al . (U.S. Pat. No. 5,019,400) was used to encapsulate the spray dried NESP powder in PLGA.
  • the protein powder was added to a polymer solution of PLGA in dichloromethane (5 - 20% w/v) to achieve a protein solids content in the microparticles ranging from 1 - 5% (w/w) .
  • a container of ethanol was frozen by immersion in liquid nitrogen, and overlayed with a layer of liquid nitrogen prior to the spray freezing step.
  • the suspension of protein powder in polymer solution was pumped via a syringe pump to an ultrasonic nozzle placed above the frozen bath of ethanol.
  • the suspension was atomized into droplets that froze upon contact with the liquid nitrogen and settled onto the surface of the frozen ethanol, forming microparticles.
  • the frozen bath was transferred to -80 °C for 72 hours to allow the ethanol to melt and extract the polymer solvent from the microparticles .
  • the resulting slurry of microparticles in ethanol was cold- filtered (0.65 ⁇ m PTFE) and the collected microparticles were lyophilized. Following lyophilization the microparticles (0.53% NESP peptide content) were sieved (125 ⁇ m mesh size) prior to characterization.
  • NESP protein powders were characterized as described in Example 2, with the results for the NESP/trehalose already presented there.
  • NESP/ammonium sulfate (AS) was characterized by size exclusion chromatography under native conditions; monomer percent was significantly decreased post spray drying, by 2.5%. This was a dimer confirmed by sodium dodecyl polyacrylamide gel electrophoresis (SDS-PAGE) , and demonstrated to be non-reducible, using silver stain.
  • the particle size distribution of the NESP/AS protein powder was determined by Fraunhoffer diffraction to have mean volume distribution of 4.3 ⁇ m.
  • the particle size of the NESP-containing microparticles fabricated by spray freezing for 28 unique lots of various formulations ranged from 20 to 45 ⁇ m for the mean of the volume distribution.
  • the residual methylene chloride levels were all ⁇ 500 ppm for the 10 lots evaluated.
  • the post-encapsulation integrity of NESP within these microparticles was assessed by extracting the protein and analyzing the extracts as described in Example 2. Protein recovery was quantitative and integrity (monomer %) was 97.2 ⁇ 2%, each lot characterized in at least duplicate.
  • the extracts from 9 select formulations were additionally characterized by a radioimmunoassay, capillary electrophoresis, and peptide mapping.
  • the RIA resulted in protein recoveries consistent with the SEC results, demonstrating antibody recognizable protein.
  • Capillary electrophoresis confirmed that the glycoform distribution was unchanged from the unprocessed NESP.
  • the extent of oxidation of the protein determined from the peptide mapping ranged from 7 - 12%, un
  • Example 3 Male Sprague Dawley rats were treated as described in Example 3 with different formulations of NESP-containing microparticles fabricated by the spray freeze process as described in Example 6. Serum NESP concentration and whole blood analyses were performed through 4-6 weeks as described in Example 3.
  • Figure 5 shows the results obtained for the NESP serum levels using various copolymer formulations of Example 5. All of the copolymer formulations demonstrated a burst phase followed by a phase of zero- order release, and then a drop to below the assay quantitation limit. Increasing the lactide content decreased the NESP serum level through the zero order phase by over 100-fold. Increasing the inherent viscosity (molecular weight) likewise decreased this NESP serum level, but only by 4-fold (See Figure 6) . Both increasing the inherent viscosity and increasing the lactide content, whether by copolymer composition or polymer solution mixture, increased the duration of quantifiable serum NESP concentrations from 18 days to as long as 35 days.
  • mice Male BDF1 mice (body weight 22 g) were treated with NESP/PLGA microparticles (50:50, inherent viscosity 0.4 dL/g), in a single, subcutaneous bolus injection into the nape of the neck, at NESP doses of 6, 30 and 100 ⁇ g/kg.
  • NESP solution test groups were dosed in a single, subcutaneous bolus injection into the nape of the neck, at NESP doses of 100, 1,000 and 10,000 ⁇ g/kg.
  • the study design was such that blood was collected every 2-4 days for whole blood analysis over a 35 day period, but any individual animal was not bled more than twice in a 7 day period.
  • This example describes the double emulsion/solvent extraction and evaporation method for preparing PLGA microparticles containing NESP, and demonstrates the ability to provide for sustained release of NESP in vivo .
  • NESP N-(peptide concentration) formulated with 20 mM sodium phosphate, pH 6.0
  • formulation 2 5.2 mg/mL NESP (peptide concentration) formulated with 20 mM sodium phosphate, 105 mg/mL 2-hydroxypropyl ⁇ -cyclodextrin, pH 6.0.
  • Microparticles containing the above NESP formulations were prepared from unblocked PLGA (50:50, inherent viscosity 0.2, 11 kD) obtained from Boehringer Ingelheim Chemicals, Inc., Montvale, N.J. The double emulsion followed by solvent extraction and evaporation method was used as described below.
  • the cured emulsion was washed with water twice by transferring the solution to two 50 mL tubes, centrifuging at 500 g-force for 30 seconds, decanting to a volume of 10 mLs, and repeating.
  • the final suspension was transferred into vials and lyophilized.
  • the final dry powder was sieved (180 ⁇ m mesh size) prior to characterization by methods described in Example 2.
  • the process provided quantitative encapsulation efficiency, poor product yield (50%), large particle size (120 ⁇ m) , and acceptable residual methylene chloride levels (near 500 ppm) .
  • the post- encapsulation integrity of NESP within these microparticles was assessed by extracting the protein and analyzing the extracts as described in Example 2. Protein recovery was quantitative and integrity (monomer %) was 97.5% ⁇ 0.01% for formulation (1), and 96.7 ⁇ 0.3% for formulation (2); each lot was characterized in triplicate.
  • Example 9 Male Sprague Dawley rats were treated as described in Example 3 with the two formulations of NESP-containing microparticles fabricated by the double emulsion process. Serum NESP levels demonstrated a burst phase followed by a phase of zero-order release, and then a drop to below the assay quantitation limit after 18 days for formulation 1 and after 22 days for formulation 2. The pharmacodynamic effect as measured by hemoglobin elevated above baseline, lasted for 25 and >28 days (end of study) for formulations (1) and (2), respectively (See Figure 8) . EXAMPLE 9
  • This example describes the preparation of microparticles containing leptin and demonstrates the ability of leptin-containing microparticles to provide for sustained release of leptin in vivo .
  • Leptin-containing microparticles were prepared using the procedure described in Example 1, and then characterized as described in Example 2. It was determined that protein recovery was >95% and the integrity was >98%. The process provided high encapsulation efficiency (85-95%), good product yield (75-85%) , low burst ( ⁇ 15%) , acceptable particle size (-35 ⁇ m) , and acceptable residual solvent levels. It was further demonstrated that the formulation exhibited good storage stability.
  • “Jn vivo" bioactivity of leptin-containing microparticles were evaluated in normal rats. A total leptin dose of 50 mg/kg (corresponding to -150 mg microparticles/kg) were administered as a single injection at day 0. In addition, the following control groups were included: daily leptin bolus (5 mg/kg/day x 10 days); dose dump control (50 mg/kg at day 0); placebo microparticles administered at day ) ; and daily placebo injection control. Animals were weighed daily, and serum samples collected periodically to assess the serum leptin concentration.
  • Serum leptin levels are shown in Figure 9. The leptin concentration in the serum remains above baseline for approximately 5 days. Weight loss is presented in Figure 10. % body weight loss relative to buffer control was determined for a 30 day period. Daily injection of a leptin solution resulted in 4-6% weight loss relative to placebo controls . A single injection of leptin-containing microparticles resulted in 9-10% weight loss relative to placebo microparticles, and resulted in sustained weight loss in rats for a 25 day period.
  • This example describes a method for preparing protein loaded microparticles; specifically, the preparation of poly (D, L-lactide-co-glycolide) microspheres containing NESP, using spray drying for the microparticle preparation step.
  • NESP was formulated at 46% NESP, 29% sodium phosphate salts, 25% trehalose (w/w/w) and spray dried on a pilot plant scale spray dryer (Niro Mobile MinorTM) using the following conditions: feed rate 8.0 ml/min, atomization gas 0.33 lbs/min (two-fluid nozzle), inlet temperature 200°C, outlet temperature 100°C, drying gas flow rate 2.0 lbs/min.
  • feed rate 8.0 ml/min feed rate 8.0 ml/min
  • atomization gas 0.33 lbs/min (two-fluid nozzle)
  • inlet temperature 200°C outlet temperature 100°C
  • drying gas flow rate 2.0 lbs/min The protein powder was collected and characterized as described in Example 11 below.
  • the protein powder was added to a PLGA (high molecular weight, (inherent viscosity 0.49 dL/g), 50% lactide) in dichloromethane/ethanol polymer solution (10% w/v) and the resulting suspension was spray dried on a pilot plant scale spray dryer (Niro Mobile MinorTM) using the following conditions: feed rate 12 ml/min, atomization (ultrasonic nozzle) 1.3 watts, inlet gas temperature 55°C, outlet temperature 28°C, drying gas flow rate 1.2 lbs/min.
  • the resulting NESP-containing microparticles (0.53% NESP) were then collected and secondary drying was performed as described in Example 4 to reduce residual solvent concentrations to less than 1000 ppm.
  • the resulting microparticles were characterized after sieving (125 ⁇ m mesh size) .
  • This example describes various characterization experiments performed on the spray dried NESP/trehalose protein powder and the NESP- containing microparticles described in Example 10.
  • the NESP/trehalose protein powder was characterized by size exclusion chromatography under native conditions; monomer percent was 99.8% post spray drying (100% for un-processed material) . No additional aggregate was observed by sodium dodecyl polyacrylamide gel electrophoresis (SDS-PAGE) , using silver stain.
  • the protein powder was analyzed by reverse phase high performance liquid chromatography (RP-HPLC) ; no change from the unprocessed NESP was observed.
  • RP-HPLC reverse phase high performance liquid chromatography
  • the protein powder was also characterized by an HPLC glycoform assay and isoelectric focusing gel electrophoresis (IEF) no change in glycoform distribution was observed.
  • the particle size distribution of the protein powder was determined by Fraunhoffer diffraction to have a mean size of 2.5 ⁇ m (volume distribution)
  • the NESP-containing microparticles were determined by Fraunhoffer diffraction to have a mean size of 45 ⁇ 1 ⁇ m (volume distribution) . Residual solvent concentrations of dichloromethane and ethanol were determined by head space gas chromatography to be 638 ppm and ⁇ 100 ppm, respectively.
  • the post-encapsulation integrity of NESP within these microparticles was assessed by extracting the protein as described in Example 2 and analyzing the extracts via anion exchange and size exclusion HPLC under native conditions. Protein was quantitated and integrity determined by anion exchange in series with size exclusion HPLC. Protein recovery was quantitative (>99%) and protein integrity was 98.6 ⁇ 0.3% monomeric by size exclusion HPLC. No additional aggregates were observed by sodium dodecyl polyacrylamide gel electrophoresis (SDS-PAGE) , using silver stain. The NESP microparticle protein extract was analyzed by reverse phase high performance liquid chromatography (RP-HPLC) ; no change from the NESP protein powder was observed. The NESP microparticle protein extract was also characterized by an HPLC glycoform assay and isoelectric focusing gel electrophoresis (IEF) no change in glycoform distribution was observed.
  • RP-HPLC reverse phase high performance liquid chromatography
  • Example 10 This example demonstrates the ability of NESP- containing microparticles prepared in Example 10 to provide for sustained release of NESP in vivo .
  • Example 3 Male Sprague Dawley rats were treated as described in Example 3 with NESP-containing microparticles fabricated as described in Example 10. Serum NESP concentration and whole blood analyses were performed through 4-8 weeks as described in Example 3.
  • NESP serum levels from a single injection of NESP-containing microparticles were > 1 ng/mL for 20 days (See Figure 11) .
  • the NESP alone given as a single bolus had elevated serum levels for 11 days (See Figure 11) .
  • the NESP-containing microparticles elevated hematocrit above baseline for 34 days (See Figure 12) .
  • the NESP bolus had elevated hematocrit for 20 days (See Figure 12) .
  • Example 10 This example demonstrates the ability of NESP- containing microparticles prepared in Example 10 to provide for sustained release of NESP in vivo .
  • Example 3 Male NIHRNU-M Nude rats were treated as described in Example 3 with NESP-containing microparticles fabricated as described in Example 10. Serum NESP concentration and whole blood analyses were performed through 4-8 weeks as described in Example 3.
  • NESP serum levels from a single injection of NESP-containing microparticles were > 1 ng/mL for 21 days (See Figure 13) .
  • the NESP alone given as a single bolus had elevated serum levels for less than 11 days (See Figure 13) .
  • the NESP-containing microparticles elevated hematocrit above baseline for 44 days days (See Figure 14) .
  • the NESP bolus had elevated hematocrit for 18 days (See Figure 14) .
  • the present NESP may be prepared according to the above incorporated-by-reference PCT Application No. US94/02957.
  • the present recombinant methionyl-human-OB protein may be prepared according to the above incorporated-by-reference PCT publication, WO 96/05309 at pages 151-159.
  • a human OB protein was used which has (as compared to the amino acid sequence at page 158) a lysine at position 35 instead of an arginine, and an isoleucine at position 74 instead of an isoleucine.
  • Other recombinant human OB proteins may be prepared according to methods known generally in the art of expression of proteins using recombinant DNA technology.

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Abstract

L'invention concerne une composition permettant la libération prolongée d'une nouvelle protéine biologiquement active stimulant l'érythropoïétine (NESP), et des procédés améliorés permettant de fabriquer cette composition. La composition comprend des microparticules polymères à l'intérieur desquelles des particules de la nouvelle protéine ont été dispersées. Le procédé amélioré consiste à utiliser un mélange de cosolvants de manière à retirer plus rapidement et plus efficacement des restes de solvants polymères au cours d'un processus de séchage.
EP00973798A 1999-10-22 2000-10-23 Microparticules biodegradables contenant une nouvelle proteine stimulant l'erythropoietine Withdrawn EP1221942A1 (fr)

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2000-02-22
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