WO2007128724A1 - Dpp iv inhibitor formulations - Google Patents

Dpp iv inhibitor formulations Download PDF

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Publication number
WO2007128724A1
WO2007128724A1 PCT/EP2007/054204 EP2007054204W WO2007128724A1 WO 2007128724 A1 WO2007128724 A1 WO 2007128724A1 EP 2007054204 W EP2007054204 W EP 2007054204W WO 2007128724 A1 WO2007128724 A1 WO 2007128724A1
Authority
WO
WIPO (PCT)
Prior art keywords
pharmaceutical composition
diluent
disintegrant
lubricant
binder
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.)
Ceased
Application number
PCT/EP2007/054204
Other languages
English (en)
French (fr)
Inventor
Anja Kohlrausch
Patrick Romer
Gerd Seiffert
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.)
Boehringer Ingelheim International GmbH
Boehringer Ingelheim Pharma GmbH and Co KG
Boehringer Ingelheim Pharmaceuticals Inc
Original Assignee
Boehringer Ingelheim International GmbH
Boehringer Ingelheim Pharma GmbH and Co KG
Boehringer Ingelheim Pharmaceuticals Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=36972901&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2007128724(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority to JP2009508327A priority Critical patent/JP5478244B2/ja
Priority to KR1020157022377A priority patent/KR101710881B1/ko
Priority to HK09110601.1A priority patent/HK1130442B/xx
Priority to AT07728658T priority patent/ATE480228T1/de
Priority to CN2007800162273A priority patent/CN101437493B/zh
Priority to KR20087026969A priority patent/KR101478983B1/ko
Priority to EA200802184A priority patent/EA016559B1/ru
Priority to MX2018008133A priority patent/MX384206B/es
Priority to BRPI0711179-7A priority patent/BRPI0711179B1/pt
Priority to DE602007009091T priority patent/DE602007009091D1/de
Priority to KR1020147011768A priority patent/KR20140063896A/ko
Priority to HR20100507T priority patent/HRP20100507T1/hr
Priority to MX2011004033A priority patent/MX358617B/es
Application filed by Boehringer Ingelheim International GmbH, Boehringer Ingelheim Pharma GmbH and Co KG, Boehringer Ingelheim Pharmaceuticals Inc filed Critical Boehringer Ingelheim International GmbH
Priority to SI200730434T priority patent/SI2023902T1/sl
Priority to CA2649922A priority patent/CA2649922C/en
Priority to NZ572862A priority patent/NZ572862A/en
Priority to MEP-2010-172A priority patent/ME01170B/me
Priority to AU2007247193A priority patent/AU2007247193B2/en
Priority to MX2008013958A priority patent/MX2008013958A/es
Priority to DK07728658.1T priority patent/DK2023902T3/da
Priority to BRPI0722388-9A priority patent/BRPI0722388B1/pt
Priority to EP07728658A priority patent/EP2023902B8/en
Priority to PL07728658T priority patent/PL2023902T4/pl
Publication of WO2007128724A1 publication Critical patent/WO2007128724A1/en
Priority to NO20084256A priority patent/NO343067B1/no
Priority to IL195030A priority patent/IL195030A/en
Anticipated expiration legal-status Critical
Priority to IL212841A priority patent/IL212841A0/en
Ceased legal-status Critical Current

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    • A61K31/495—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with two or more nitrogen atoms as the only ring heteroatoms, e.g. piperazine or tetrazines
    • A61K31/505—Pyrimidines; Hydrogenated pyrimidines, e.g. trimethoprim
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    • A61K31/52—Purines, e.g. adenine
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Definitions

  • the present invention relates to pharmaceutical compositions of selected DPP IV inhibitors, their preparation and their use to treat selected medical conditions.
  • DPP-IV dipeptidyl peptidase IV
  • CD26 The enzyme DPP-IV (dipeptidyl peptidase IV) also known as CD26 is a serine protease known to lead to the cleavage of a dipeptide from the N-terminal end of a number of proteins having at their N-terminal end a prolin or alanin residue. Due to this property DPP-IV inhibitors interfere with the plasma level of bioactive peptides including the peptide GLP-1 and are considered to be promising drugs for the treatment of diabetes mellitus.
  • DPP-IV inhibitors with a primary or secondary amino group show incompatibilities, degradation problems, or extraction problems with a number of customary excipients such as microcrystalline cellulose, sodium starch glycolate, croscarmellose sodium, tartaric acid, citric acid, glucose, fructose, saccharose, lactose, maltodextrines.
  • customary excipients such as microcrystalline cellulose, sodium starch glycolate, croscarmellose sodium, tartaric acid, citric acid, glucose, fructose, saccharose, lactose, maltodextrines.
  • the compounds themselves are very stable, they react with many excipients used in solid dosage forms and with impurities of excipients, especially in tight contact provided in tablets and at high excipient/drug ratios.
  • a pharmaceutical composition according to the present invention is intended for the treatment of to achieve glycemic control in a type 1 or type 2 diabetes mellitus patient and comprises a DPP-IV inhibitor with an amino group, especially a free or primary amino group, as an active ingredient, a first and second diluent, a binder, a disintegrant and a lubricant.
  • An additional disintegrant and an additional glidant are a further option.
  • the compositions can be used to treat rheumatoid arthritis, obesity and osteoporosis as well as to support allograft transplantation.
  • Diluents suitable for a pharmaceutical composition according to the invention are cellulose powder, dibasic calciumphosphate anhydrous, dibasic calciumphosphate dihydrate, erythritol, low substituted hydroxypropyl cellulose, mannitol, pregelatinized starch or xylitol. Among those diluents mannitol and pregelatinized starch are preferred.
  • Diluents preferred as the second diluent are the above mentioned diluents pregelatinized starch and low-substituted hydroxypropylcellulose (L-HPC) which show additional binder properties.
  • Lubricants suitable for a pharmaceutical composition according to the invention are talc, polyethyleneglycol, calcium behenate, calcium stearate, hydrogenated castor oil or magnesium stearate.
  • the preferred lubricant is magnesium stearate.
  • Binders suitable for a pharmaceutical composition according to the invention are copovidone (copolymerisates of vinylpyrrolidon with other vinylderivates), hydroxypropyl methylcellulose (HPMC), hydroxypropylcellulose (HPC), polyvinylpyrrolidon (povidone), pregelatinized starch, low-substituted hydroxypropylcellulose (L-HPC), copovidone and pregelatinized starch being preferred.
  • binders pregelatinized starch and L-HPC show additional diluent and disintegrant properties and can also be used as the second diluent or the disintegrant.
  • Disintegrants suitable for a pharmaceutical composition according to the present invention are corn starch, crospovidone, low-substituted hydroxypropylcellulose (L- HPC) or pregelatinized starch, corn starch being preferred.
  • An exemplary composition according to the present invention comprises the diluent mannitol, pregelatinized starch as a diluent with additional binder properties, the binder copovidone, the disintegrant corn starch, and magnesium stearate as the lubricant.
  • Dosage forms prepared with a pharmaceutical compositions according to the present invention contain active ingredients in dosage ranges of 0.1-100 mg. Preferred dosages are 0.5 mg, 1 mg, 2.5 mg, 5 mg and 10 mg.
  • Typical pharmaceutical compositions comprise (% by weight) 0.5-20 % active ingredient
  • Preferred pharmaceutical compositions comprise (% by weight)
  • compositions according to the invention are intended for oral use and can be used in the dosage form of a capsule, a tablet or a film-coated tablet.
  • the film coat represents 2-4%, preferably 3% of the composition and comprises a film-forming agent, a plasticizer, a glidant and optionally one or more pigments.
  • An exemplary coat composition may comprise hydroxypropylmethyl- cellulose (HPMC), polyethylene glycol (PEG), talc, titanium dioxide and optionally iron oxide.
  • HPMC hydroxypropylmethyl- cellulose
  • PEG polyethylene glycol
  • talc titanium dioxide
  • titanium dioxide optionally iron oxide
  • DPP-IV inhibitors with a primary amino group and salts thereof such as any DPP-IV inhibitor and salt thereof defined by formula (I)
  • R1 is ([1 ,5]naphthyhdin-2-yl)methyl, (quinazolin-2-yl)methyl], (quinoxalin-6- yl)methyl, (4-Methyl-quinazolin-2-yl)methyl, 2-Cyano-benzyl, (3-Cyano-quinolin-2- yl)methyl, (3-Cyano-pyridin-2-yl)methyl, (4-Methyl-pyrimidin-2-yl)methyl, or (4,6- Dimethyl-pyrimidin-2-yl)methyl, and R2 is 3-(R)-amino-piperidin-1-yl, (2-amino-2- methyl-propyl)-methylamino or (2-(S)-amino-propyl)-methylamino.
  • Preferred DPP IV inhibitor compounds are the following compounds and salts thereof:
  • compositions according to the invention can be prepared by a wet granulation process.
  • Alternative methods for granulation of active ingredient and excipients with a granulation liquid are fluid bed granulation or one-pot granulation.
  • the granulation liquid is a solvent such as water, ethanol, methanol, isopropanol, acetone, preferably purified water, and contains a binder such as copovidone.
  • the solvent is a volatile component, which does not remain in the final product.
  • the active ingredient and the other excipients with exception of the lubricant are premixed and granulated with the aqueous granulation liquid using a high shear granulator.
  • the wet granulation step is followed by an optional wet sieving step, drying and dry sieving of the granules. For example a fluid bed dryer can then be used for drying.
  • the dried granules are sieved through an appropriate sieve.
  • a suitable conventional blender such as a free fall blender followed by addition of the lubricant such as magnesium stearate and final blending in the blender.
  • an exemplary wet granulation process for the preparation of a pharmaceutical composition comprises a. dissolving a binder such as copovidone in a solvent such as purified water at ambient temperature to produce a granulation liquid; b. blending a DPP-IV inhibitor, a diluent, and a disintegrant in a suitable mixer, to produce a pre-mix; c. moistening the pre-mix with the granulation liquid and subsequently granulating the moistened pre-mix for example in a high shear mixer; d. optionally sieving the granulated pre-mix through a sieve with a mesh size of at least 1.0 mm and preferably 3 mm; e.
  • part of the exipients such as part of a disintegrant (e.g. corn starch) or a diluent (e.g. pregelatinized starch) or an additional disintegrant (crospovidone) can be added extragranular prior to final blending of step g.
  • a disintegrant e.g. corn starch
  • a diluent e.g. pregelatinized starch
  • an additional disintegrant crospovidone
  • the granulate produced in steps a to e is produced in a one pot high shear granulation process and subsequent drying in a one pot granulator.
  • the final blend is further filled into capsules.
  • the final blend is further compressed into tablets of the target tablet core weight with appropriate size and crushing strength, using an appropriate tablet press.
  • a coating suspension is prepared and the compressed tablet cores are coated with the coating suspension to a weight gain of about 2-4 %, preferably about 3%, using a standard film coater.
  • the film-coating solvent is a volatile component, which does not remain in the final product.
  • Example 1 Formulation for direct compression
  • An active DPP IV inhibitor ingredient with a primary amino group and all other excipients with exception of magnesium stearate are blended in a high shear blender. This pre-mix is sieved through a 1 mm sieve. After addition of magnesium stearate the pre-mix is blended in a free fall blender to produce the final blend. The final blend is compressed into tablets using a suitable tablet press.
  • the following compositions can be obtained:
  • Example 2 Alternative formulation for direct compression An active DPP IV inhibitor ingredient with a primary amino group and all other excipients with exception of magnesium stearate are blended in a high shear blender. This pre-mix is sieved through a 1 mm sieve. After addition of magnesium stearate the pre-mix is blended in a free fall blender to produce the final blend. The final blend is compressed into tablets using a suitable tablet press.
  • the following compositions can be obtained:
  • Copovidone is dissolved in purified water at ambient temperature to produce a granulation liquid.
  • An active DPP IV inhibitor ingredient with a primary amino group, mannitol and part of the pregelatinized starch are blended in a suitable mixer, to produce a pre-mix.
  • the pre-mix is moistened with the granulation liquid and subsequently granulated.
  • the moist granulate is optionally sieved through a sieve with a mesh size of 1.6-3.0 mm.
  • the granulate is dried at 55 0 C in a suitable dryer to a residual moisture content corresponding to 2-5 % loss on drying.
  • the dried granulate is sieved through a sieve with a mesh size of 1.0 mm.
  • the granulate is blended with part of the pregelatinized starch in a suitable mixer.
  • Magnesium stearate is added to this blend after passing through a 1.0 mm sieve for delumping.
  • the final blend is produced by final blending in a suitable mixer and compressed into tablets.
  • the following tablet composition can be obtained:
  • Example 4 Coated tablet formulation
  • Copovidone is dissolved in purified water at ambient temperature to produce a granulation liquid.
  • An active DPP IV inhibitor ingredient with a primary amino group, mannitol, pregelatinized starch and corn starch are blended in a suitable mixer to produce the pre-mix.
  • the pre-mix is moistened with the granulation liquid and subsequently granulated using a high shear mixer.
  • the moist granulate is optionally sieved through a sieve with a mesh size of 1.6-3.0 mm.
  • the granulate is dried at about 60 0 C in a fluid bed dryer until a loss on the drying value of 2-4 % is obtained.
  • the Final Blend is compressed into tablet cores.
  • Hydroxypropyl methylcellulose, polyethylene glycol, talc, titanium dioxide and iron oxide are suspended in purified water in a suitable mixer at ambient temperature to produce a coating suspension.
  • the tablet cores are coated with the coating suspension to a weight gain of about 3 % to produce film-coated tablets.
  • the following tablet compositions can be obtained:
  • Copovidone is dissolved in purified water at ambient temperature to produce a granulation liquid.
  • An active DPP IV inhibitor ingredient with a primary amino group, mannitol and pregelatinized starch are blended in a suitable mixer to produce a pre- mix.
  • the pre-mix is moistened with the granulation liquid and subsequently granulated.
  • the moist granulate is optionally sieved through a suitable sieve.
  • the granulate is dried at about 50 0 C in a suitable dryer until a loss on drying value of 3- 5% is obtained.
  • the dried granulate is sieved through a sieve with a mesh size of 1.0 mm.
  • Magnesium stearate is passed through a 1.0 mm sieve and added to the granulate. Subsequently the final blend is produced by final blending in a suitable blender and the final blend is compressed into tablets.
  • the following tablet compositions can be obtained:
  • Copovidone is dissolved in purified water at ambient temperature to produce a granulation liquid.
  • An active DPP IV inhibitor ingredient with a primary amino group and a part of mannitol, pregelatinized starch and corn starch are blended in a suitable mixer, to produce a pre-mix.
  • the pre-mix is moistened with the granulation liquid and subsequently granulated.
  • the moist granulate is sieved through a suitable sieve.
  • the granulate is dried at about 60 0 C inlet air temperature in a fluid bed dryer until a loss on drying value of 1-4 % is obtained.
  • the dried granulate is sieved through a sieve with a mesh size of 1.0 mm.
  • Magnesium stearate is passed through a sieve for delumping and added to the granulate. Additionally the remaining part of the exipients are added extragranular at this process step. Subsequently the final blend is produced by final blending in a suitable blender and compressed into tablet cores.

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PCT/EP2007/054204 2006-05-04 2007-04-30 Dpp iv inhibitor formulations Ceased WO2007128724A1 (en)

Priority Applications (26)

Application Number Priority Date Filing Date Title
PL07728658T PL2023902T4 (pl) 2006-05-04 2007-04-30 Formulacje zawierające inhibitory DPP-IV
SI200730434T SI2023902T1 (sl) 2006-05-04 2007-04-30 DPP IV inhibitorske formulacije
HK09110601.1A HK1130442B (en) 2006-05-04 2007-04-30 Dpp iv inhibitor formulations
AT07728658T ATE480228T1 (de) 2006-05-04 2007-04-30 Dpp-iv-inhibitor-formulierungen
CN2007800162273A CN101437493B (zh) 2006-05-04 2007-04-30 二肽基肽酶iv抑制剂制剂
KR20087026969A KR101478983B1 (ko) 2006-05-04 2007-04-30 Ｄｐｐ ｉｖ 억제제 제형
EA200802184A EA016559B1 (ru) 2006-05-04 2007-04-30 Фармацевтические композиции с ингибиторами dpp iv
MX2018008133A MX384206B (es) 2006-05-04 2007-04-30 Formulaciones de inhibidores de dpp iv
BRPI0711179-7A BRPI0711179B1 (pt) 2006-05-04 2007-04-30 Composição farmacêutica contendo composto inibidor de dpp iv e processo para a sua preparação
DE602007009091T DE602007009091D1 (de) 2006-05-04 2007-04-30 Dpp-iv-inhibitor-formulierungen
KR1020147011768A KR20140063896A (ko) 2006-05-04 2007-04-30 Ｄｐｐ ｉｖ 억제제 제형
HR20100507T HRP20100507T1 (hr) 2006-05-04 2007-04-30 Formulacije inhibitora dpp iv
MX2011004033A MX358617B (es) 2006-05-04 2007-04-30 Formulaciones de inhibidores de dpp iv.
JP2009508327A JP5478244B2 (ja) 2006-05-04 2007-04-30 Ｄｐｐ ｉｖインヒビター製剤
CA2649922A CA2649922C (en) 2006-05-04 2007-04-30 Dpp iv inhibitor formulations
DK07728658.1T DK2023902T3 (da) 2006-05-04 2007-04-30 DPP-IV-inhibitor-formuleringer
EP07728658A EP2023902B8 (en) 2006-05-04 2007-04-30 Dpp iv inhibitor formulations
MEP-2010-172A ME01170B (me) 2006-05-04 2007-04-30 Formulacije dpp iv inhibitora
AU2007247193A AU2007247193B2 (en) 2006-05-04 2007-04-30 DPP IV inhibitor formulations
MX2008013958A MX2008013958A (es) 2006-05-04 2007-04-30 Formulaciones de inhibidores de dpp iv.
KR1020157022377A KR101710881B1 (ko) 2006-05-04 2007-04-30 Ｄｐｐ ｉｖ 억제제 제형
BRPI0722388-9A BRPI0722388B1 (pt) 2006-05-04 2007-04-30 Forma de dosagem oral farmacêutica sólida de composto inibidor de dpp iv
NZ572862A NZ572862A (en) 2006-05-04 2007-04-30 DPP IV inhibitor formulations which comprise mannitol, pregelatinised starch, copovidone, corn starch and magnesium stearate
NO20084256A NO343067B1 (no) 2006-05-04 2008-10-10 DPP IV-hemmerformuleringer, fremgangsmåte for fremstilling av slike samt doseformer inneholdende slike
IL195030A IL195030A (en) 2006-05-04 2008-10-30 Dpp iv inhibitor formulations
IL212841A IL212841A0 (en) 2006-05-04 2011-05-12 Dpp iv inhibitor formulations

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EP06009201A EP1852108A1 (en) 2006-05-04 2006-05-04 DPP IV inhibitor formulations
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JP (8) JP5478244B2 (enExample)
KR (5) KR101855323B1 (enExample)
CN (2) CN101437493B (enExample)
AR (2) AR060755A1 (enExample)
AT (1) ATE480228T1 (enExample)
AU (1) AU2007247193B2 (enExample)
BR (2) BRPI0722388B1 (enExample)
CA (1) CA2649922C (enExample)
CL (2) CL2012002522A1 (enExample)
CY (2) CY1111354T1 (enExample)
DE (1) DE602007009091D1 (enExample)
DK (3) DK2283819T3 (enExample)
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PE (2) PE20110666A1 (enExample)
PL (3) PL2023902T4 (enExample)
PT (2) PT2023902E (enExample)
RS (2) RS53570B1 (enExample)
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SI (2) SI2023902T1 (enExample)
TW (2) TWI474843B (enExample)
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