WO2019012552A1 - Compositions of ferric organic compounds - Google Patents
Compositions of ferric organic compounds Download PDFInfo
- Publication number
- WO2019012552A1 WO2019012552A1 PCT/IN2018/050441 IN2018050441W WO2019012552A1 WO 2019012552 A1 WO2019012552 A1 WO 2019012552A1 IN 2018050441 W IN2018050441 W IN 2018050441W WO 2019012552 A1 WO2019012552 A1 WO 2019012552A1
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- WO
- WIPO (PCT)
- Prior art keywords
- ferric citrate
- ferric
- core
- surface area
- pharmaceutical composition
- Prior art date
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- 239000000203 mixture Substances 0.000 title claims abstract description 36
- 150000002894 organic compounds Chemical class 0.000 title claims abstract description 25
- NPFOYSMITVOQOS-UHFFFAOYSA-K iron(III) citrate Chemical compound [Fe+3].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NPFOYSMITVOQOS-UHFFFAOYSA-K 0.000 claims abstract description 69
- 229960002413 ferric citrate Drugs 0.000 claims abstract description 67
- 239000000546 pharmaceutical excipient Substances 0.000 claims abstract description 25
- 239000007884 disintegrant Substances 0.000 claims abstract description 20
- 239000008194 pharmaceutical composition Substances 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims description 28
- 238000007908 dry granulation Methods 0.000 claims description 15
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 13
- 239000011230 binding agent Substances 0.000 claims description 12
- 238000005550 wet granulation Methods 0.000 claims description 12
- 229960000913 crospovidone Drugs 0.000 claims description 10
- 239000007888 film coating Substances 0.000 claims description 10
- 238000009501 film coating Methods 0.000 claims description 10
- 235000013809 polyvinylpolypyrrolidone Nutrition 0.000 claims description 10
- 229920000523 polyvinylpolypyrrolidone Polymers 0.000 claims description 10
- 239000000314 lubricant Substances 0.000 claims description 9
- 239000011248 coating agent Substances 0.000 claims description 4
- 238000000576 coating method Methods 0.000 claims description 4
- FWZTTZUKDVJDCM-CEJAUHOTSA-M disodium;(2r,3r,4s,5s,6r)-2-[(2s,3s,4s,5r)-3,4-dihydroxy-2,5-bis(hydroxymethyl)oxolan-2-yl]oxy-6-(hydroxymethyl)oxane-3,4,5-triol;iron(3+);oxygen(2-);hydroxide;trihydrate Chemical compound O.O.O.[OH-].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Na+].[Na+].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 FWZTTZUKDVJDCM-CEJAUHOTSA-M 0.000 claims description 4
- 229940031703 low substituted hydroxypropyl cellulose Drugs 0.000 claims description 4
- 229920002678 cellulose Polymers 0.000 claims description 3
- 239000001913 cellulose Substances 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- -1 glidants Substances 0.000 claims description 3
- 229940032961 iron sucrose Drugs 0.000 claims description 2
- 229960004158 sucroferric oxyhydroxide Drugs 0.000 claims description 2
- 239000004480 active ingredient Substances 0.000 abstract description 2
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 16
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 description 15
- 239000008187 granular material Substances 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 238000009472 formulation Methods 0.000 description 9
- 239000008213 purified water Substances 0.000 description 9
- 239000001863 hydroxypropyl cellulose Substances 0.000 description 8
- 229940071676 hydroxypropylcellulose Drugs 0.000 description 8
- 235000019359 magnesium stearate Nutrition 0.000 description 8
- 238000004090 dissolution Methods 0.000 description 7
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 description 7
- 239000004615 ingredient Substances 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- 235000013539 calcium stearate Nutrition 0.000 description 6
- 239000008116 calcium stearate Substances 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 238000003801 milling Methods 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 6
- 229910019142 PO4 Inorganic materials 0.000 description 5
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 5
- 208000020832 chronic kidney disease Diseases 0.000 description 5
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 5
- 239000010452 phosphate Substances 0.000 description 5
- 239000008186 active pharmaceutical agent Substances 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 238000005469 granulation Methods 0.000 description 4
- 230000003179 granulation Effects 0.000 description 4
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 description 4
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 description 4
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 208000010444 Acidosis Diseases 0.000 description 3
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 3
- 206010027417 Metabolic acidosis Diseases 0.000 description 3
- 229920000881 Modified starch Polymers 0.000 description 3
- 239000003085 diluting agent Substances 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 229940088679 drug related substance Drugs 0.000 description 3
- 201000005991 hyperphosphatemia Diseases 0.000 description 3
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 229940124531 pharmaceutical excipient Drugs 0.000 description 3
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 3
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 3
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- 229920002785 Croscarmellose sodium Polymers 0.000 description 2
- 229920000168 Microcrystalline cellulose Polymers 0.000 description 2
- 208000001647 Renal Insufficiency Diseases 0.000 description 2
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 2
- 238000005056 compaction Methods 0.000 description 2
- 229960001681 croscarmellose sodium Drugs 0.000 description 2
- 235000010947 crosslinked sodium carboxy methyl cellulose Nutrition 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 239000002706 dry binder Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 208000028208 end stage renal disease Diseases 0.000 description 2
- 201000000523 end stage renal failure Diseases 0.000 description 2
- 239000005414 inactive ingredient Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 208000017169 kidney disease Diseases 0.000 description 2
- 201000006370 kidney failure Diseases 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 235000019813 microcrystalline cellulose Nutrition 0.000 description 2
- 239000008108 microcrystalline cellulose Substances 0.000 description 2
- 229940016286 microcrystalline cellulose Drugs 0.000 description 2
- 229940069328 povidone Drugs 0.000 description 2
- 238000009491 slugging Methods 0.000 description 2
- 229920003109 sodium starch glycolate Polymers 0.000 description 2
- 239000008109 sodium starch glycolate Substances 0.000 description 2
- 229940079832 sodium starch glycolate Drugs 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- OYPRJOBELJOOCE-BKFZFHPZSA-N Calcium-45 Chemical compound [45Ca] OYPRJOBELJOOCE-BKFZFHPZSA-N 0.000 description 1
- PTHCMJGKKRQCBF-UHFFFAOYSA-N Cellulose, microcrystalline Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC)C(CO)O1 PTHCMJGKKRQCBF-UHFFFAOYSA-N 0.000 description 1
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- 241000237858 Gastropoda Species 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 229920000084 Gum arabic Polymers 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 235000010489 acacia gum Nutrition 0.000 description 1
- 239000000205 acacia gum Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 235000010443 alginic acid Nutrition 0.000 description 1
- 239000000783 alginic acid Substances 0.000 description 1
- 229920000615 alginic acid Polymers 0.000 description 1
- 229960001126 alginic acid Drugs 0.000 description 1
- 150000004781 alginic acids Chemical class 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 235000010980 cellulose Nutrition 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000000378 dietary effect Effects 0.000 description 1
- 235000015872 dietary supplement Nutrition 0.000 description 1
- 239000003937 drug carrier Substances 0.000 description 1
- MVPICKVDHDWCJQ-UHFFFAOYSA-N ethyl 3-pyrrolidin-1-ylpropanoate Chemical compound CCOC(=O)CCN1CCCC1 MVPICKVDHDWCJQ-UHFFFAOYSA-N 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 210000001035 gastrointestinal tract Anatomy 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 238000001631 haemodialysis Methods 0.000 description 1
- 230000000322 hemodialysis Effects 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- WBJZTOZJJYAKHQ-UHFFFAOYSA-K iron(3+) phosphate Chemical class [Fe+3].[O-]P([O-])([O-])=O WBJZTOZJJYAKHQ-UHFFFAOYSA-K 0.000 description 1
- SHXXPRJOPFJRHA-UHFFFAOYSA-K iron(iii) fluoride Chemical compound F[Fe](F)F SHXXPRJOPFJRHA-UHFFFAOYSA-K 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000006186 oral dosage form Substances 0.000 description 1
- 239000008203 oral pharmaceutical composition Substances 0.000 description 1
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 238000009490 roller compaction Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 210000002966 serum Anatomy 0.000 description 1
- 235000010413 sodium alginate Nutrition 0.000 description 1
- 239000000661 sodium alginate Substances 0.000 description 1
- 229940005550 sodium alginate Drugs 0.000 description 1
- 229940045902 sodium stearyl fumarate Drugs 0.000 description 1
- 230000002037 soft tissue calcification Effects 0.000 description 1
- 229940032147 starch Drugs 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 235000012222 talc Nutrition 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 235000010493 xanthan gum Nutrition 0.000 description 1
- 239000000230 xanthan gum Substances 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 229940082509 xanthan gum Drugs 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/33—Heterocyclic compounds
- A61K31/555—Heterocyclic compounds containing heavy metals, e.g. hemin, hematin, melarsoprol
-
- 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
- A61K9/20—Pills, tablets, discs, rods
- A61K9/2004—Excipients; Inactive ingredients
- A61K9/2022—Organic macromolecular compounds
- A61K9/205—Polysaccharides, e.g. alginate, gums; Cyclodextrin
- A61K9/2054—Cellulose; Cellulose derivatives, e.g. hydroxypropyl methylcellulose
-
- 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
- A61K9/20—Pills, tablets, discs, rods
- A61K9/2072—Pills, tablets, discs, rods characterised by shape, structure or size; Tablets with holes, special break lines or identification marks; Partially coated tablets; Disintegrating flat shaped forms
- A61K9/2077—Tablets comprising drug-containing microparticles in a substantial amount of supporting matrix; Multiparticulate tablets
-
- 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
- A61K9/20—Pills, tablets, discs, rods
- A61K9/2095—Tabletting processes; Dosage units made by direct compression of powders or specially processed granules, by eliminating solvents, by melt-extrusion, by injection molding, by 3D printing
Definitions
- This invention relates to pharmaceutical composition of pharmaceutical grade ferric organic compounds, such as Ferric citrate.
- Ferric iron containing compounds are useful in the treatment of a number of disorders, including, but not limited to, hyperphosphatemia and metabolic acidosis.
- Ferric iron containing compounds existing in the art are for example Ferric chloride, Ferric oxide, Ferric fluoride, and Ferric citrate. Elevated amounts of phosphate in the blood can be removed by administering compounds such as Ferric citrate. Once in solution, the ferric iron binds phosphate, and the ferric phosphate compounds precipitate in the gastrointestinal tract, resulting in effective removal of dietary phosphate from the body. It is also believed that the absorbed citrate from Ferric citrate is converted to bicarbonate which corrects metabolic acidosis, a condition common in renal failure patients.
- Ferric citrate has the following structure, and can be referred to as FCT.
- the novel form of Ferric citrate has the formula C 6 H 5 O 7 Fe and has novel physical properties as determined by dissolution rates, and has a molecular weight of 244.94 g/mole.
- Ferric citrate is approved in 2014 in USA, and the NDA applicant is Keryx Pharmaceuticals.
- Pharmaceutical grade Ferric citrate is suitable for treating hyperphosphatemia, or other disorders characterized by high serum phosphate levels. Specifically, for treating subjects or patients with various renal diseases; e.g., End Stage Renal Diseases (ESRD), Chronic Kidney Disease (CKD) or other related kidney diseases, or subjects and patients who are on dialysis but not limited to hemodialysis.
- Ferric citrate is characterized as a light brown to beige powder, odorless and slightly ferruginous tasting. According to the Merck Index, Ferric citrate is slowly but completely soluble in cold water and readily soluble in hot water but diminishes in solubility with age.
- US 5,753,706 discloses that Ferric citrate compounds can be used to control phosphate metabolism and prevent metabolic acidosis in patients. Ferric citrate compounds can be used with patients suffering from renal failure associated with hyperphosphatemia or patients predisposed to development of a hyperphosphatemic condition. Ferric citrate also is used as a food supplement and additive.
- US 6,903,235 discloses that Ferric citrate is commercially available in the form of a combination of iron and citric acid of indefinite composition. It explains that the indefinite composition is likely due to difficulties encountered in its preparation but that those knowledgeable in the art understand and necessarily accept that commercially available Ferric citrate contains different molar ratios of iron and citric acid and also contains different amounts of water.
- WO 2004/074444 discloses processes for making Ferric organic compounds, such as Ferric citrate, with enhanced dissolution rates
- WO 2007/022435 is a continuation-in-part of WO 2004/074444 and discloses processes for making Ferric organic compounds soluble over a wide pH range and having a large surface area.
- WO 2007/089577 is directed to methods of treating soft tissue calcification using Ferric organic compounds, such as a Ferric citrate.
- WO 2007/089571 is directed to methods of treating chronic kidney disease using Ferric organic compounds, such as Ferric citrate.
- US 9,387,191/US 2013/274328 A1/US 2016/0263075 A relates to a composition of Ferric citrate comprising Pregelatinized starch, a lubricant and coating.
- IN 2016/28011726 which is an equivalent of US 9,387,191 relates to Ferric citrate tablet wherein the mean surface area to mass ratio of said granule particles is equal to or greater than 1 m 2 /g.
- IN 305/MUMNP/2012 which is an equivalent of US 9,387,191 relates to a tablet containing Ferric citrate with a mean surface area to mass ratio of 1 m 2 /g, and a binder, with LOD limitation.
- US 2016/0263038 which is assigned to Keryx pharma relates to FCT composition containing Pregelatinized starch.
- US 2009/0186939 which is an equivalent of US 7,767,851 relates to Ferric citrate having BET surface area ⁇ 16m 2 /g.
- WO2016/162794 relates to FCT tablet, wherein Ferric citrate having a specific surface area less than 16m 2 /g.
- WO2016/162888 relates to Ferric citrate having a BET active surface area of less than 16 m 2 /g.
- WO 2015/110968 relates to Ferric citrate having a BET active surface area in the range of 1-15 m 2 /g.
- WO 2015/198304 discloses FCT tablet preparation and process for preparation FCT composition using wet granulation.
- IN241/MUM/2014 / IN 201627024694 relates to Ferric citrate having a BET active surface area in the range of 1-15 m 2 /gm.
- IN 996/DEL/2015 relates to pharmaceutical grade Ferric citrate having a BET active surface area of less than 16 m 2 /g and a mean dissolution rate of 4 to 9 mg/cm 2 /min.
- IN 253106 which is an equivalent of WO 2007/022435 relates to Ferric citrate having intrinsic dissolution of 1.9 to 4 mg/cm 2 /min, and BET active surface area greater than 16 m 2 /g.
- the main aspect of the invention is to provide a pharmaceutical composition comprising Ferric citrate, along with disintegrant and other pharmaceutically acceptable excipients.
- the composition disintegrates within 15 minutes, and the BET surface area of Ferric citrate of the composition is the in the range of 6-12 m 2 /g.
- the other aspect of the present invention is to provide an oral pharmaceutical composition of Ferric organic compound such as Ferric citrate.
- the other aspect of the invention provides a pharmaceutical composition comprising: Ferric organic compound; and a disintegrant.
- the invention provides a pharmaceutical composition in the form of a tablet that comprises Ferric organic compound, a disintegrant selected from crospovidone, low substituted hydroxypropyl cellulose, cross linked cellulose, sodium starch glycolate, and microcrystalline cellulose or a combination thereof, and one or more pharmaceutically acceptable excipients, for example, a binder, a lubricant or any combination thereof.
- a disintegrant selected from crospovidone, low substituted hydroxypropyl cellulose, cross linked cellulose, sodium starch glycolate, and microcrystalline cellulose or a combination thereof
- one or more pharmaceutically acceptable excipients for example, a binder, a lubricant or any combination thereof.
- the invention provides a pharmaceutical composition consisting of a tablet that comprises a powder blend or granules comprising Ferric organic compound; a disintegrant, and one or more pharmaceutically acceptable excipients, for example, a binder, and a lubricant.
- composition of the invention disintegrates within 15 minutes.
- the pharmaceutical composition is directed to a tablet comprising Ferric citrate having a BET surface area in the range of 6-12 m 2 /g.
- the present invention relates to the pharmaceutical composition
- the pharmaceutical composition comprising Ferric organic compound, and disintegrant, which is prepared by either dry granulation or wet granulation.
- the Ferric organic compounds which include Ferric citrate, Iron Sucrose, Sucroferric Oxyhydroxide, preferably Ferric citrate.
- the pharmaceutical composition is directed to a tablet comprising Ferric citrate, having a BET surface area of compound is in the range of 6-12 m 2 /g.
- the tablet can include at least 70 weight percent Ferric citrate, at least 80 weight percent Ferric citrate, or at least 90 weight percent Ferric citrate.
- the disintegrant can be one or more of crospovidone, low substituted hydroxypropyl cellulose, cross linked cellulose, microcrystalline cellulose, crosspovidone, sodium starch glycolate or a combination thereof.
- the tablet can include various additional components including, for example, one or more binders and/or one or more lubricants, and optionally other pharmaceutical excipients.
- composition excipients include excipients, for example, diluents, glidants etc.... Specific examples of pharmaceutically acceptable carriers and excipients that may be used to formulate oral dosage forms are described in the Handbook of Pharmaceutical Excipients, American Pharmaceutical Association (1986).
- composition contains a definite composition and a definite hydrate.
- the binder can be selected from one or more of hydroxypropyl cellulose (HPC), hydroxypropylmethyl cellulose (HPMC), sodium alginate, alginic acid, guar gum, acacia gum, xanthan gum, carbopol, cellulose gum (carboxymethyl cellulose), ethyl cellulose, PVP/VA, povidone, starch (partially or fully pregelatinized starch) and methyl cellulose.
- the lubricant can be one or more of magnesium stearate, calcium stearate, sodium stearyl fumarate, polyethylene glycol (molecular weight above 3350), talc, mineral and vegetable oil.
- compositions and process for the preparation of compositions containing Ferric organic compounds which can include Ferric citrate.
- the formulations can include Ferric citrate as the active ingredient and a disintegrant.
- compositions containing Ferric organic compounds which can include Ferric citrate.
- the composition can be prepared by dry granulation, where roller compactor is widely used as one of dry granulation process.
- a dry granulation is prepared by compacting a dry powder blend of the drug and inactive tableting ingredients using roller compactor or slugging by using compression machine, milling the compacts and blending the resultant granulation with other inactive ingredients followed by lubrication. This method is commonly used for drug substance that has better or moderate compressibility but not having good flow characteristics.
- a typical granulation is prepared by blending Ferric organic compound with inactive tableting ingredients in a blender, compacting the blend using a roller compactor, milling to a desired particle size and lubrication.
- Dry granulation is usually described as a method of controlled crushing of precompacted powders densified by either slugging or passing the material between two counter-rotating rolls. More specifically, powdered components that may contain very fine particles are typically mixed prior to being compacted to yield hard slugs which are then milled and sieved before the addition of other ingredients and finally compressed into tablets.
- a wet granulation technique requires preparation of a blend, wetting the blend with a binder solution to get a wet mass, milling the wet mass into moist granules agglomerated with a binder and drying the granules, followed by further milling and blending with other inactive ingredients.
- this process of agglomeration with a binder results in a compressible granulation.
- a typical granulation is prepared in a conventional granulator, high sheer granulator or fluid bed granulator. Drying of the wet granular mass is usually achieved in a fluid bed dryer.
- this invention relates to an improved process for preparing Ferric organic compound tablets by a modified wet granulation technique; and especially, but not exclusively, tablets which have a high active matter content, in particular, tablets containing poorly compressible medicinally active matter.
- a modified wet granulation technique involves no more than the incorporation of a granulating fluid into the mixed, powdery tablet ingredients (including at least some tabletting aids) in such an amount and manner as to convert them into a uniform, moist, coherent, non-pasty mass, which then is formed into moist granules of fairly uniform size, usually by forcing the mass through a screen. Thereafter the moist granules are dried and rescreened to break down agglomerates, and finally blended with other tabletting aids so as thus to arrive at the granulate ready for tabletting.
- the invention provides a process for making the pharmaceutical compositions described herein by roller compaction process comprising the steps of weighing Ferric organic compound and excipients, screening, blending Ferric organic compound and excipients for a suitable amount of time; roller compacting the blend into ribbons and milling the ribbons into granules; blending the granules with extra-granular excipients for a suitable amount of time; compressing the blend into tablets; coating the tablets.
- the method for producing a pharmaceutical composition comprises providing an admixture of solid forms, e.g. an admixture of powdered ingredients, the admixture comprising Ferric organic compound, a disintegrant and one or more excipients selected from: a dry binder, a glidant, a diluent, a lubricant, and a filler; mixing the admixture until the admixture is substantially homogenous, and compressing/compacting the admixture into a granular form using a roller compactor using a dry granulation composition as set forth in the Examples below.
- an admixture of solid forms e.g. an admixture of powdered ingredients, the admixture comprising Ferric organic compound, a disintegrant and one or more excipients selected from: a dry binder, a glidant, a diluent, a lubricant, and a filler
- mixing the admixture until the
- the method for producing a pharmaceutical composition comprises providing an admixture of solid forms, e.g. an admixture of powdered ingredients, the admixture comprising Ferric organic compound, a disintegrant and one or more excipients selected from: a binder, a glidant, a diluent, a lubricant, and a filler; mixing the admixture until the admixture is substantially homogenous, and compressing/compacting the admixture into a granular form using a wet granulation composition as set forth in the Examples below.
- an admixture of solid forms e.g. an admixture of powdered ingredients, the admixture comprising Ferric organic compound, a disintegrant and one or more excipients selected from: a binder, a glidant, a diluent, a lubricant, and a filler
- mixing the admixture until the admixture is substantially homogen
- Example 1 Ferric citrate formulation was prepared by using dry granulation technique, where L-HPC has been used as the disintegrant.
- Example 2 Ferric citrate formulation was prepared by using dry granulation technique, where Crospovidone has been used as the disintegrant.
- Example 3 Ferric citrate formulation was prepared by using dry granulation technique, where Croscarmellose sodium has been used as the disintegrant.
- Example 4 Ferric citrate formulation was prepared by using dry granulation technique, where L-HPC has been used as the disintegrant.
- Manufacturing Process a) The drug substance and dry binder were sifted and loaded into blender and blended for about 10 min, b) The intragranular lubricant was sifted and added to above step and blended for about 5 min, c) The above material was loaded into hopper of Compactor and compacted with suitable hardness of ribbons with preset roller RPM, GAP, Vertical and horizontal feeder screw speed. d) The above flakes were milled in multimill fitted with suitable screen at suitable speed and suitable direction, e) The milled material was sifted using suitable ASTM mesh. The compaction followed by milling process will be continued till desired particle size of granules obtained.
- Example 5 Ferric citrate formulation was prepared by using wet granulation technique, where L-HPC has been used as the disintegrant.
- Example 6 Ferric citrate formulation was prepared by using wet granulation technique, where crospovidone has been used as the disintegrant.
- Example 7 Ferric citrate formulation was prepared by using wet granulation technique, where crospovidone has been used as the disintegrant.
- Example 8 Ferric citrate formulation was prepared by using wet granulation technique, where L-HPC has been used as the disintegrant.
- PROCESS a) The drug substance along with intragranular ingredients was sifted through # 20 ASTM. b) The binding agent was dissolved in purified water under stirring to get clear solution. c) Step no 1 material was loaded into top bowl of fluid bed processer and coated with step no b binder solution until consistence granules obtained. The set bed temperature during the process is 40 ° C ⁇ 10 ° C. d) The above material was dried at set inlet temperature 50 ° C ⁇ 10 ° C till target LOD achieved. e) The dried granules were sifted through # 18 ASTM mesh and retained are milled in multimill fitted with suitable screen at optimum speed and milled granules were sifted through # 18 ASTM.
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Abstract
The invention relates to Ferric organic compound containing compositions. The pharmaceutical compositions of the invention which include Ferric citrate as the active ingredient, a disintegrant, and one or more pharmaceutically acceptable excipients, along with an optional film coat wherein the Ferric citrate has BET surface area of 6 - 12 m2/g.
Description
This invention relates to pharmaceutical composition of pharmaceutical grade ferric organic compounds, such as Ferric citrate.
Ferric iron containing compounds are useful in the treatment of a number of disorders, including, but not limited to, hyperphosphatemia and metabolic acidosis. Ferric iron containing compounds existing in the art are for example Ferric chloride, Ferric oxide, Ferric fluoride, and Ferric citrate. Elevated amounts of phosphate in the blood can be removed by administering compounds such as Ferric citrate. Once in solution, the ferric iron binds phosphate, and the ferric phosphate compounds precipitate in the gastrointestinal tract, resulting in effective removal of dietary phosphate from the body. It is also believed that the absorbed citrate from Ferric citrate is converted to bicarbonate which corrects metabolic acidosis, a condition common in renal failure patients.
Ferric citrate has the following structure, and can be referred to as FCT.
The novel form of Ferric citrate has the formula C6H5O7Fe and has novel physical properties as determined by dissolution rates, and has a molecular weight of 244.94 g/mole. Ferric citrate is approved in 2014 in USA, and the NDA applicant is Keryx Pharmaceuticals. Pharmaceutical grade Ferric citrate is suitable for treating hyperphosphatemia, or other disorders characterized by high serum phosphate levels. Specifically, for treating subjects or patients with various renal diseases; e.g., End Stage Renal Diseases (ESRD), Chronic Kidney Disease (CKD) or other related kidney diseases, or subjects and patients who are on dialysis but not limited to hemodialysis. Ferric citrate is characterized as a light brown to beige powder, odorless and slightly ferruginous tasting. According to the Merck Index, Ferric citrate is slowly but completely soluble in cold water and readily soluble in hot water but diminishes in solubility with age.
US 5,753,706 discloses that Ferric citrate compounds can be used to control phosphate metabolism and prevent metabolic acidosis in patients. Ferric citrate compounds can be used with patients suffering from renal failure associated with hyperphosphatemia or patients predisposed to development of a hyperphosphatemic condition. Ferric citrate also is used as a food supplement and additive. US 6,903,235 discloses that Ferric citrate is commercially available in the form of a combination of iron and citric acid of indefinite composition. It explains that the indefinite composition is likely due to difficulties encountered in its preparation but that those knowledgeable in the art understand and necessarily accept that commercially available Ferric citrate contains different molar ratios of iron and citric acid and also contains different amounts of water.
WO 2004/074444 discloses processes for making Ferric organic compounds, such as Ferric citrate, with enhanced dissolution rates, WO 2007/022435 is a continuation-in-part of WO 2004/074444 and discloses processes for making Ferric organic compounds soluble over a wide pH range and having a large surface area. WO 2007/089577 is directed to methods of treating soft tissue calcification using Ferric organic compounds, such as a Ferric citrate. WO 2007/089571 is directed to methods of treating chronic kidney disease using Ferric organic compounds, such as Ferric citrate. Where in US 7,767,851 relates to Ferric citrate having intrinsic dissolution of 1.9 to 4 mg/cm2/min, US 8,299,298 B2/ US 8,754,258 B2 relate to Ferric citrate having BET active surface area of at least 16 sq. m/g, US 8,338,642 B2/ US 8,901,349 B2/ US 8,609,896 B2 relate to Ferric citrate having BET active surface area greater than 16 sq. m/g. US 8,754,257 B2, US 9,328,133 and US 8,093,423 relate to FCT having intrinsic dissolution rate of 1.88-4.0 mg/cm2/min. US 8,754,258 B2/ US 8,846,976 B2/ US 9,050,316 B2 relate to FCT having intrinsic dissolution rate of at least 1.88 mg/cm2/min.
US 9,387,191/US 2013/274328 A1/US 2016/0263075 A relates to a composition of Ferric citrate comprising Pregelatinized starch, a lubricant and coating. IN 2016/28011726 which is an equivalent of US 9,387,191 relates to Ferric citrate tablet wherein the mean surface area to mass ratio of said granule particles is equal to or greater than 1 m2/g. IN 305/MUMNP/2012 which is an equivalent of US 9,387,191 relates to a tablet containing Ferric citrate with a mean surface area to mass ratio of 1 m2/g, and a binder, with LOD limitation. US 2016/0263038 which is assigned to Keryx pharma relates to FCT composition containing Pregelatinized starch. US 2009/0186939 which is an equivalent of US 7,767,851 relates to Ferric citrate having BET surface area ≥16m2/g. WO2016/162794 relates to FCT tablet, wherein Ferric citrate having a specific surface area less than 16m2/g. WO2016/162888 relates to Ferric citrate having a BET active surface area of less than 16 m2/g. WO 2015/110968 relates to Ferric citrate having a BET active surface area in the range of 1-15 m2/g. WO 2015/198304 discloses FCT tablet preparation and process for preparation FCT composition using wet granulation. IN241/MUM/2014 / IN 201627024694 relates to Ferric citrate having a BET active surface area in the range of 1-15 m2/gm. IN 996/DEL/2015 relates to pharmaceutical grade Ferric citrate having a BET active surface area of less than 16 m2/g and a mean dissolution rate of 4 to 9 mg/cm2/min. IN 253106 which is an equivalent of WO 2007/022435 relates to Ferric citrate having intrinsic dissolution of 1.9 to 4 mg/cm2/min, and BET active surface area greater than 16 m2/g.
Accordingly, there exists a need for improved/technologically advanced/economically feasible/scalable compositions of Ferric organic compounds or Ferric citrate for human use.
The main aspect of the invention is to provide a pharmaceutical composition comprising Ferric citrate, along with disintegrant and other pharmaceutically acceptable excipients. According to other object of invention, the composition disintegrates within 15 minutes, and the BET surface area of Ferric citrate of the composition is the in the range of 6-12 m2/g.
The other aspect of the present invention is to provide an oral pharmaceutical composition of Ferric organic compound such as Ferric citrate. The other aspect of the invention provides a pharmaceutical composition comprising: Ferric organic compound; and a disintegrant.
In another aspect, the invention provides a pharmaceutical composition in the form of a tablet that comprises Ferric organic compound, a disintegrant selected from crospovidone, low substituted hydroxypropyl cellulose, cross linked cellulose, sodium starch glycolate, and microcrystalline cellulose or a combination thereof, and one or more pharmaceutically acceptable excipients, for example, a binder, a lubricant or any combination thereof.
In yet another aspect, the invention provides a pharmaceutical composition consisting of a tablet that comprises a powder blend or granules comprising Ferric organic compound; a disintegrant, and one or more pharmaceutically acceptable excipients, for example, a binder, and a lubricant.
In another aspect the pharmaceutical composition of the invention disintegrates within 15 minutes.
In another aspect, the pharmaceutical composition is directed to a tablet comprising Ferric citrate having a BET surface area in the range of 6-12 m2/g.
The present invention relates to the pharmaceutical composition comprising Ferric organic compound, and disintegrant, which is prepared by either dry granulation or wet granulation.
In one aspect, the Ferric organic compounds, which include Ferric citrate, Iron Sucrose, Sucroferric Oxyhydroxide, preferably Ferric citrate.
In other aspect, the pharmaceutical composition is directed to a tablet comprising Ferric citrate, having a BET surface area of compound is in the range of 6-12 m2/g.
In another aspect, the tablet can include at least 70 weight percent Ferric citrate, at least 80 weight percent Ferric citrate, or at least 90 weight percent Ferric citrate.
In yet another aspect, the disintegrant can be one or more of crospovidone, low substituted hydroxypropyl cellulose, cross linked cellulose, microcrystalline cellulose, crosspovidone, sodium starch glycolate or a combination thereof.
In another aspect, the tablet can include various additional components including, for example, one or more binders and/or one or more lubricants, and optionally other pharmaceutical excipients.
Pharmaceutical excipients include excipients, for example, diluents, glidants etc…. Specific examples of pharmaceutically acceptable carriers and excipients that may be used to formulate oral dosage forms are described in the Handbook of Pharmaceutical Excipients, American Pharmaceutical Association (1986).
Pharmaceutical grade ferric citrate contains a definite composition and a definite hydrate.
In yet another aspect, the binder can be selected from one or more of hydroxypropyl cellulose (HPC), hydroxypropylmethyl cellulose (HPMC), sodium alginate, alginic acid, guar gum, acacia gum, xanthan gum, carbopol, cellulose gum (carboxymethyl cellulose), ethyl cellulose, PVP/VA, povidone, starch (partially or fully pregelatinized starch) and methyl cellulose. The lubricant can be one or more of magnesium stearate, calcium stearate, sodium stearyl fumarate, polyethylene glycol (molecular weight above 3350), talc, mineral and vegetable oil.
In one aspect, disclosed herein are compositions and process for the preparation of compositions containing Ferric organic compounds, which can include Ferric citrate. In various aspects, the formulations can include Ferric citrate as the active ingredient and a disintegrant.
In another aspect, disclosed herein are pharmaceutical compositions and a process for the preparation of compositions containing Ferric organic compounds which can include Ferric citrate.
According to one aspect, the composition can be prepared by dry granulation, where roller compactor is widely used as one of dry granulation process.
In another aspect a dry granulation is prepared by compacting a dry powder blend of the drug and inactive tableting ingredients using roller compactor or slugging by using compression machine, milling the compacts and blending the resultant granulation with other inactive ingredients followed by lubrication. This method is commonly used for drug substance that has better or moderate compressibility but not having good flow characteristics.
In yet another aspect, a typical granulation is prepared by blending Ferric organic compound with inactive tableting ingredients in a blender, compacting the blend using a roller compactor, milling to a desired particle size and lubrication. Dry granulation is usually described as a method of controlled crushing of precompacted powders densified by either slugging or passing the material between two counter-rotating rolls. More specifically, powdered components that may contain very fine particles are typically mixed prior to being compacted to yield hard slugs which are then milled and sieved before the addition of other ingredients and finally compressed into tablets. Although dry granulation would in many cases appear to be the best way to produce products such as tablets containing APIs, it has been relatively little used because of the challenges in producing the desired kind of granules as well as managing the granulated material in the manufacturing process. Known dry granulation methods, as well as the known issues related to them are well described in scientific articles, such as the review article "Roll compaction / dry granulation: pharmaceutical applications" written by Peter Kleinebudde and published in European Journal of Pharmaceutics and Biopharmaceutics 58 (2004) at pages 317-326.
In one aspect, a wet granulation technique requires preparation of a blend, wetting the blend with a binder solution to get a wet mass, milling the wet mass into moist granules agglomerated with a binder and drying the granules, followed by further milling and blending with other inactive ingredients. For drugs that are not compressible and lack required flow characteristics, this process of agglomeration with a binder results in a compressible granulation. A typical granulation is prepared in a conventional granulator, high sheer granulator or fluid bed granulator. Drying of the wet granular mass is usually achieved in a fluid bed dryer.
In yet another aspect, this invention relates to an improved process for preparing Ferric organic compound tablets by a modified wet granulation technique; and especially, but not exclusively, tablets which have a high active matter content, in particular, tablets containing poorly compressible medicinally active matter. There is much art and skill in practicing the wet granulation technique; but in outline, it involves no more than the incorporation of a granulating fluid into the mixed, powdery tablet ingredients (including at least some tabletting aids) in such an amount and manner as to convert them into a uniform, moist, coherent, non-pasty mass, which then is formed into moist granules of fairly uniform size, usually by forcing the mass through a screen. Thereafter the moist granules are dried and rescreened to break down agglomerates, and finally blended with other tabletting aids so as thus to arrive at the granulate ready for tabletting.
According to another aspect, the invention provides a process for making the pharmaceutical compositions described herein by roller compaction process comprising the steps of weighing Ferric organic compound and excipients, screening, blending Ferric organic compound and excipients for a suitable amount of time; roller compacting the blend into ribbons and milling the ribbons into granules; blending the granules with extra-granular excipients for a suitable amount of time; compressing the blend into tablets; coating the tablets.
According to yet another embodiment, the method for producing a pharmaceutical composition comprises providing an admixture of solid forms, e.g. an admixture of powdered ingredients, the admixture comprising Ferric organic compound, a disintegrant and one or more excipients selected from: a dry binder, a glidant, a diluent, a lubricant, and a filler; mixing the admixture until the admixture is substantially homogenous, and compressing/compacting the admixture into a granular form using a roller compactor using a dry granulation composition as set forth in the Examples below.
According to yet another embodiment, the method for producing a pharmaceutical composition comprises providing an admixture of solid forms, e.g. an admixture of powdered ingredients, the admixture comprising Ferric organic compound, a disintegrant and one or more excipients selected from: a binder, a glidant, a diluent, a lubricant, and a filler; mixing the admixture until the admixture is substantially homogenous, and compressing/compacting the admixture into a granular form using a wet granulation composition as set forth in the Examples below.
The following examples illustrate various aspects of the present invention. They are not to be construed to limit the claims in any manner whatsoever.
Example 1: Ferric citrate formulation was prepared by using dry granulation technique, where L-HPC has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.0 | 88.50 |
L-HPC | 20.0 | 1.77 |
Calcium Stearate | 10.0 | 0.88 |
Extragranular Part | ||
L-HPC | 80.0 | 7.08 |
Calcium Stearate | 20.0 | 1.77 |
Tablet weight | 1130 | 100.00 |
Film coating | ||
Opadry | 20.0 | |
Purified water | QS | |
Total | 1150.0 | 100.00 |
Example 2: Ferric citrate formulation was prepared by using dry granulation technique, where Crospovidone has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.0 | 88.50 |
Hydroxypropyl methyl cellulose | 20.0 | 1.77 |
Magnesium Stearate | 10.0 | 0.88 |
Extragranular Part | ||
Crospovidone | 80.0 | 7.08 |
Magnesium Stearate | 20.0 | 1.77 |
Tablet weight | 1130 | 100.00 |
Film coating | ||
Opadry | 20.0 | |
Purified water | QS | |
Total | 1150.0 | 100.00 |
Example 3: Ferric citrate formulation was prepared by using dry granulation technique, where Croscarmellose sodium has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.0 | 88.50 |
Hydroxypropyl methyl cellulose | 20.0 | 1.77 |
Magnesium Stearate | 10.0 | 0.88 |
Extragranular Part | ||
Croscarmellose sodium | 80.0 | 7.08 |
Magnesium Stearate | 20.0 | 1.77 |
Tablet weight | 1130 | 100.00 |
Film coating | ||
Opadry | 20.0 | |
Purified water | QS | |
Total | 1150.0 | 100.00 |
Example 4: Ferric citrate formulation was prepared by using dry granulation technique, where L-HPC has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.0 | 88.50 |
Hydroxypropyl cellulose | 20.0 | 1.77 |
Magnesium Stearate | 10.0 | 0.88 |
Extragranular Part | ||
L-HPC | 80.0 | 7.08 |
Magnesium Stearate | 20.0 | 1.77 |
Tablet weight | 1130 | 100.00 |
Film coating | ||
Opadry | 20.0 | |
Purified water | QS | |
Total | 1150.0 | 100.00 |
Manufacturing Process:
a) The drug substance and dry binder were sifted and loaded into blender and blended for about 10 min,
b) The intragranular lubricant was sifted and added to above step and blended for about 5 min,
c) The above material was loaded into hopper of Compactor and compacted with suitable hardness of ribbons with preset roller RPM, GAP, Vertical and horizontal feeder screw speed.
d) The above flakes were milled in multimill fitted with suitable screen at suitable speed and suitable direction,
e) The milled material was sifted using suitable ASTM mesh. The compaction followed by milling process will be continued till desired particle size of granules obtained.
f) The above material loaded in blender and blended for 5 min,
g) The extragranular material was sifted through # 40 ASTM and loaded to above step and blended for 5 min,
h) The above lubricated material compressed into tablets with suitable punches,
i) The core tablets are coated with opadry and evaluated for physicochemical properties.
a) The drug substance and dry binder were sifted and loaded into blender and blended for about 10 min,
b) The intragranular lubricant was sifted and added to above step and blended for about 5 min,
c) The above material was loaded into hopper of Compactor and compacted with suitable hardness of ribbons with preset roller RPM, GAP, Vertical and horizontal feeder screw speed.
d) The above flakes were milled in multimill fitted with suitable screen at suitable speed and suitable direction,
e) The milled material was sifted using suitable ASTM mesh. The compaction followed by milling process will be continued till desired particle size of granules obtained.
f) The above material loaded in blender and blended for 5 min,
g) The extragranular material was sifted through # 40 ASTM and loaded to above step and blended for 5 min,
h) The above lubricated material compressed into tablets with suitable punches,
i) The core tablets are coated with opadry and evaluated for physicochemical properties.
Example 5: Ferric citrate formulation was prepared by using wet granulation technique, where L-HPC has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.00 | 90.9 |
L- Hydroxypropyl cellulose | 10.00 | 0.9 |
Hydroxypropyl cellulose | 20.00 | 1.8 |
Extragranular Part | ||
L- Hydroxypropyl cellulose | 55.00 | 5.0 |
Calcium Stearate | 15.00 | 1.4 |
Tablet weight | 1100.00 | 100.00 |
Film coating | ||
Opadry | 30.00 | |
Purified water | QS | |
Total | 1130.0 | - |
Example 6: Ferric citrate formulation was prepared by using wet granulation technique, where crospovidone has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.00 | 90.9 |
Hydroxypropyl cellulose | 20.00 | 1.8 |
Extragranular Part | ||
Crospovidone | 65.00 | 5.9 |
Calcium Stearate | 15.00 | 1.4 |
Tablet weight | 1100.00 | 100.00 |
Film coating | ||
Opadry | 30.00 | |
Purified water | QS | |
Total | 1130.0 | - |
Example 7: Ferric citrate formulation was prepared by using wet granulation technique, where crospovidone has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.00 | 90.91 |
Crospovidone | 5.00 | 0.45 |
Hypermellose | 15.00 | 1.36 |
Extragranular Part | ||
Crospovidone | 60.00 | 5.45 |
Calcium Stearate | 20.00 | 1.82 |
Tablet weight | 1100.00 | 100.00 |
Film coating | ||
Opadry | 30.00 | |
Purified water | QS | |
Total | 1130.0 | - |
Example 8: Ferric citrate formulation was prepared by using wet granulation technique, where L-HPC has been used as the disintegrant.
Excipients | mg/unit | % w/w |
Core Tablet | ||
Ferric citrate | 1000.00 | 90.91 |
Povidone | 30.00 | 2.73 |
Extragranular Part | ||
L-Hydroxy propyl cellulose | 50.00 | 4.55 |
Magnesium Stearate | 20.00 | 1.82 |
Tablet weight | 1100.00 | 100.00 |
Film coating | ||
Opadry | 30.00 | |
Purified water | QS | |
Total | 1130.0 | - |
PROCESS:
a) The drug substance along with intragranular ingredients was sifted through # 20 ASTM.
b) The binding agent was dissolved in purified water under stirring to get clear solution.
c) Step no 1 material was loaded into top bowl of fluid bed processer and coated with step no b binder solution until consistence granules obtained. The set bed temperature during the process is 40 ° C± 10 ° C.
d) The above material was dried at set inlet temperature 50 ° C± 10 ° C till target LOD achieved.
e) The dried granules were sifted through # 18 ASTM mesh and retained are milled in multimill fitted with suitable screen at optimum speed and milled granules were sifted through # 18 ASTM.
f) The shifted material was loaded in blender and blended for 5 min.
g) The extragranular material was sifted through # 40 ASTM and loaded to above step and blended for 5 min.
h) The above lubricated material was compressed into tablets.
i) The core tablets were coated with opadry and evaluated for physicochemical properties.
a) The drug substance along with intragranular ingredients was sifted through # 20 ASTM.
b) The binding agent was dissolved in purified water under stirring to get clear solution.
c) Step no 1 material was loaded into top bowl of fluid bed processer and coated with step no b binder solution until consistence granules obtained. The set bed temperature during the process is 40 ° C± 10 ° C.
d) The above material was dried at set inlet temperature 50 ° C± 10 ° C till target LOD achieved.
e) The dried granules were sifted through # 18 ASTM mesh and retained are milled in multimill fitted with suitable screen at optimum speed and milled granules were sifted through # 18 ASTM.
f) The shifted material was loaded in blender and blended for 5 min.
g) The extragranular material was sifted through # 40 ASTM and loaded to above step and blended for 5 min.
h) The above lubricated material was compressed into tablets.
i) The core tablets were coated with opadry and evaluated for physicochemical properties.
Claims (6)
- A pharmaceutical composition comprising: (a) a core comprising Ferric organic compound, disintegrant selected from the group comprising of crospovidone, low substituted hydroxypropyl cellulose, and cross linked cellulose, or a combination thereof and one or more pharmaceutically acceptable excipients (b) optionally a coating the core with a film coating material.
- According to claim 1, the Ferric organic compound is selected from the group comprising of Ferric citrate, Iron Sucrose, Sucroferric Oxyhydroxide, preferably Ferric citrate.
- According to claim 1, pharmaceutically acceptable excipients include binders, glidants, lubricants, fillers and combinations thereof.
- According to claim 1 the pharmaceutical composition is prepared using wet granulation or dry granulation techniques.
- A Ferric citrate composition comprising: (a) a core comprising disintegrant selected from the group consisting of crosspovidone, low substituted hydroxypropyl cellulose, and cross linked cellulose, and a combination thereof, and one or more pharmaceutically acceptable excipients (b) optionally coating the core with a film coating material, wherein the Ferric citrate has BET surface area of 6 - 12 m2/gThis is a sample Claim.Since separate searches and examinations are required for distinctly different inventions, additional fees are required if the international search or international preliminary examination is to cover two or more inventions (or groups of inventions linked as just described).
- A pharmaceutical composition comprising Ferric citrate having BET surface area of 6-12 m2/g, wherein the composition is prepared by dry granulation or wet granulation, wherein the finished product disintegrates within 15 minutes.
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Cited By (2)
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CN114392249A (en) * | 2022-01-13 | 2022-04-26 | 上海医药集团青岛国风药业股份有限公司 | Enteric-coated pellet of polysaccharide-iron compound and powder direct-compression tablet |
WO2022251563A1 (en) * | 2021-05-27 | 2022-12-01 | Keryx Biopharmaceuticals, Inc. | Pediatric formulations of ferric citrate |
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WO2004074444A2 (en) * | 2003-02-19 | 2004-09-02 | Globoasia Llc | Ferric organic compounds, uses thereof and methods of making same |
WO2015110968A1 (en) * | 2014-01-23 | 2015-07-30 | Lupin Limited | Pharmaceutical grade ferric citrate and method for its production |
WO2016162794A1 (en) * | 2015-04-08 | 2016-10-13 | Leiutis Pharmaceuticals Pvt Ltd | Pharmaceutical compositions of ferric citrate |
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2018
- 2018-07-07 WO PCT/IN2018/050441 patent/WO2019012552A1/en active Application Filing
Patent Citations (3)
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WO2004074444A2 (en) * | 2003-02-19 | 2004-09-02 | Globoasia Llc | Ferric organic compounds, uses thereof and methods of making same |
WO2015110968A1 (en) * | 2014-01-23 | 2015-07-30 | Lupin Limited | Pharmaceutical grade ferric citrate and method for its production |
WO2016162794A1 (en) * | 2015-04-08 | 2016-10-13 | Leiutis Pharmaceuticals Pvt Ltd | Pharmaceutical compositions of ferric citrate |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022251563A1 (en) * | 2021-05-27 | 2022-12-01 | Keryx Biopharmaceuticals, Inc. | Pediatric formulations of ferric citrate |
CN114392249A (en) * | 2022-01-13 | 2022-04-26 | 上海医药集团青岛国风药业股份有限公司 | Enteric-coated pellet of polysaccharide-iron compound and powder direct-compression tablet |
CN114392249B (en) * | 2022-01-13 | 2023-09-12 | 上海医药集团青岛国风药业股份有限公司 | Enteric-coated pellet and powder direct compression tablet of polysaccharide-iron compound |
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