WO2006003152A1 - GRANULES COMPRISING A ß-LACTAM ANTIBIOTIC - Google Patents

GRANULES COMPRISING A ß-LACTAM ANTIBIOTIC Download PDF

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Publication number
WO2006003152A1
WO2006003152A1 PCT/EP2005/053036 EP2005053036W WO2006003152A1 WO 2006003152 A1 WO2006003152 A1 WO 2006003152A1 EP 2005053036 W EP2005053036 W EP 2005053036W WO 2006003152 A1 WO2006003152 A1 WO 2006003152A1
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WO
WIPO (PCT)
Prior art keywords
lactam antibiotic
granules
antibiotic
volume
lactam
Prior art date
Application number
PCT/EP2005/053036
Other languages
French (fr)
Inventor
Marinus Petrus Wilhelmus Maria Rijkers
Alexander Lucia Leonardus Duchateau
Johannes Helena Michael Mommers
Jozef Maria Mathias Boesten
Original Assignee
Dsm Ip Assets B.V.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dsm Ip Assets B.V. filed Critical Dsm Ip Assets B.V.
Priority to US11/630,270 priority Critical patent/US20070248666A1/en
Priority to ES05756680.4T priority patent/ES2531598T3/en
Priority to EP05756680.4A priority patent/EP1786548B1/en
Priority to BRPI0512933A priority patent/BRPI0512933B8/en
Publication of WO2006003152A1 publication Critical patent/WO2006003152A1/en
Priority to US12/889,307 priority patent/US20110011961A1/en

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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
    • A61K9/20—Pills, tablets, discs, rods
    • 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
    • A61K9/1682—Processes
    • A61K9/1688—Processes resulting in pure drug agglomerate optionally containing up to 5% of excipient
    • 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
    • A61K31/395—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/54—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with at least one nitrogen and one sulfur as the ring hetero atoms, e.g. sulthiame
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/22—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by pressing in moulds or between rollers

Definitions

  • the present invention relates to granules comprising a ⁇ -lactam antibiotic, to a process for the preparation thereof and to an apparatus for preparing the granules comprising the ⁇ -lactam antibiotic.
  • the preparation of a ⁇ -lactam antibiotic typically involves obtaining the ⁇ -lactam antibiotic as a crystalline powder, e.g. by crystallizing the ⁇ -lactam antibiotic from a solution, and drying the resulting crystals resulting in the powder.
  • the powder may be compressed, e.g. by roller compacting to form granules comprising compressed powder. Roller compacting of a ⁇ -lactam antibiotic is e.g. described in WO-A-9911261.
  • This object is achieved by providing granules comprising a ⁇ -lactam antibiotic, wherein CH2S(72 h ) ⁇ 50 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, wherein CH2S(72h) is the volume of H 2 S gas above said granules per kg of said ⁇ -lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0 C during 72 hours at atmospheric pressure (1 bar).
  • the granules comprising a ⁇ -lactam antibiotic according to the invention have a C H 2s(7 2h ) ⁇ 40 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(7 2h ) ⁇ 30 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(72h) ⁇ 25 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C ⁇ s ⁇ h ) ⁇ 20 ⁇ l of H 2 S gas per kg of ⁇ - lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0 C during 72 hours at atmospheric pressure (1 bar).
  • the granules comprising a ⁇ -lactam antibiotic according to the invention have a C H2 s (72h) > 1 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic.
  • C H2 S(72 h ) is determined under the following conditions: a sample of between 3.5 and 4.5 gram of said granules is kept in a closed container (volume of 20 ml) at a temperature of 22 0 C during 72 hours at atmospheric pressure (1 bar). After said 72 hours a sample of air is taken from the container and analysed by gas chromatography to determine the volume fraction of H 2 S in said sample of air.
  • the invention also provides granules comprising a ⁇ -lactam antibiotic, wherein
  • CH2S(3 h ) ⁇ 10 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, wherein CH 2 s(3h) is the volume of H 2 S gas above said granules per kg of said ⁇ -lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0 C during 3 hours at atmospheric pressure (1 bar).
  • the C H2 s(3 h) is determined under the following conditions: a sample of between 3.5 and 4.5 gram of said granules is kept in a closed container (volume of 20 ml) at a temperature of 22 0 C during 3 hours at atmospheric pressure (1 bar). After said 3 hours a sample of air is taken from the container and analysed by gas chromatography to determine the volume fraction of H 2 S in said sample of air. Said volume fraction of H 2 S gas is multiplied by the gas phase volume above the sample (i.e. volume of the container, i.e. 20 ml, minus the volume of the sample) resulting in the volume of H 2 S gas in the container.
  • the invention provides granules comprising a ⁇ - lactam antibiotic, wherein C H2 s(3 h ) ⁇ 9 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H 2s(3 h ) ⁇ 8 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(3h) ⁇ 7 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(3 h ) ⁇ 6 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s ( 3 h) ⁇ 5 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic when a sample of between 3.5 and 4.5 g of said granules is kept in
  • the granules comprising a ⁇ -lactam antibiotic according to the invention have a C H2 s(3 h ) > 1 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic.
  • Granules according to the invention may comprise auxiliaries or may be free of auxiliaries.
  • Granules according to the invention may comprise compressed ⁇ -lactam antibiotic, for instance ⁇ -lactam antibiotic compressed by roller compacting.
  • Granules according to the invention are preferably obtained by roller compacting.
  • the granules according to the invention may for instance have a bulk density of between 0.4 and 1.0 g/ml, for instance between 0.45 and 0.8 g/ml.
  • bulk density is preferably determined using USP 24, method I, (page 1913).
  • bulk density is determined using method Eur. Ph. 5.0, section 2.9.15.
  • auxiliaries may for instance be used fillers, dry binders, disintegrants, wetting agents, wet binders, lubricants, flow agents and the like.
  • auxiliaries are lactose, starches, bentonite, calcium carbonate, mannitol, microcrystalline cellulose, polysorbate, sodium lauryl sulphate, carboxymethylcellulose Na, sodium alginate, magnesium stearate, silicon dioxid, talc.
  • the granules according to the invention are free of auxiliaries.
  • the invention also provides a process for preparing granules according to the invention.
  • the invention provides a process for preparing granules comprising a ⁇ -lactam antibiotic, said process comprising feeding said ⁇ -lactam antibiotic to a roller compactor to form compacts, size- reducing, e.g. milling the compacts to produce granules, whereirtr the temperature of the ⁇ -lactam antibiotic that is fed to the roller compactor is sufficiently low that C H 2s(72 h ) ⁇ 50 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s ⁇ 72h) ⁇ 40 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(7 2h ) ⁇ 30 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(7 2h ) ⁇ 25 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic,preferably C H2S (7 2h ) ⁇ 20 ⁇ l of H
  • the invention provides a process for preparing granules comprising a ⁇ -lactam antibiotic, said process comprising feeding said ⁇ -lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the temperature of the ⁇ -lactam antibiotic that is fed to the roller compactor is sufficiently low that C H2S(3h) ⁇ 10 ⁇ l of H 2 S gas per kg of ⁇ - lactam antibiotic, preferably C H2S(3h ) ⁇ 9 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, -A-
  • the invention provides a process for preparing granules comprising a ⁇ -lactam antibiotic, said process comprising feeding said ⁇ -lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the said ⁇ -lactam antibiotic is cooled prior to said feeding.
  • the invention provides a process for preparing granules comprising a ⁇ -lactam antibiotic, said process comprising feeding said ⁇ -lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the temperature of the ⁇ -lactam antibiotic that is fed to said roller compactor is below 20 0 C, preferably below 18 0 C, more preferably bIlow 15 °C.
  • the ⁇ -lactam antibiotic is preferably fed to the roller compactor as a crystalline powder of the ⁇ -lactam antibiotic, preferably without auxiliaries. However, it is also possible to feed a mixture comprising a crystalline powder and auxiliaries to the roller compactor.
  • auxiliaries may for instance be used fillers, dry binders, disintegrants, wetting agents, wet binders, lubricants, flow agents and the like.
  • auxiliaries are lactose, starches, bentonite, calcium carbonate, mannitol, microcrystalline cellulose, polysorbate, sodium lauryl sulphate, carboxymethylcellulose Na, sodium alginate, magnesium stearate, silicon dioxid, talc.
  • the roller compactor may be operated at any suitable roller pressure, for instance between 10 and 250 kN, for instance between 50-200 kN.
  • the invention also provides a ⁇ -lactam antibiotic in compressed form wherein C H2 S(72 h > ⁇ 50 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(72h) ⁇ 40 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s (72h) ⁇ 30 ⁇ l of H 2 S gas per kg of ⁇ - lactam antibiotic, preferably C H2S( 72h) ⁇ 25 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic preferably C H2 s (72h) ⁇ 20 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0 C during 72 hours at atmospheric pressure (1 bar).
  • the invention also provides a ⁇ -lactam antibiotic in compressed form wherein
  • the C H2 s ⁇
  • the invention also provides a process for compressing a ⁇ -lactam antibiotic, said process comprising feeding said ⁇ -lactam antibiotic to a step in which the ⁇ -lactam antibiotic is compressed to form compressed ⁇ -lactam antibiotic, wherein the temperature of the ⁇ -lactam antibiotic that is fed to said step is sufficiently low that C H2 S (72h) ⁇ 50 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(72h) ⁇ 40 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2S(72h) ⁇ 30 ⁇ l of H 2 S gas per kg of ⁇ - lactam antibiotic, preferably C H2S(72h) ⁇ 25 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic,
  • the invention also provides a process for compressing a ⁇ -lactam antibiotic, said process comprising feeding said ⁇ -lactam antibiotic to a step in which the ⁇ -lactam antibiotic is compressed to form compressed ⁇ -lactam antibiotic, wherein the temperature of the ⁇ -lactam antibiotic that is fed to said step is sufficiently low that CH 2 S( 3 I I ) ⁇ 10 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H 2S( 3h > ⁇ 9 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(3 h ) ⁇ 8 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, C H 2S(3h ) ⁇ 7 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s(3h) ⁇ 6 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic, preferably C H2 s ( 3
  • the process comprises cooling the ⁇ -lactam antibiotic prior to said feeding. In an embodiment, the process comprises feeding said ⁇ -lactam antibiotic to a step in which the ⁇ -lactam antibiotic is compressed to form compressed ⁇ -lactam antibiotic, wherein the ⁇ -lactam antibiotic is cooled prior to said feeding.
  • the temperature of the ⁇ -lactam antibiotic that is fed to said step is below 20 0 C, preferably below 18 0 C, more preferably below 15 0 C.
  • the invention also provides an apparatus comprising
  • a means for compressing the cooled antibiotic wherein said (i) cooler is arranged such that the antibiotic can be cooled prior to feeding the antibiotic to (ii) the means for compressing the antibiotic,
  • said means for compressing the antibiotic is a roller compactor.
  • said apparatus further comprises a dryer for drying the ⁇ -lactam antibiotic, said dryer arranged such that the dried antibiotic can be fed to the cooler.
  • the ⁇ -lactam antibiotic is not limited to a specific type of ⁇ -lactam antibiotic. It may for instance be a penicillin, for instance ampicillin or amoxicillin, or a cephalosporin, for instance cephalexin, cefadroxil, cephradin, or cefalcor.
  • Cephalexin may be in any suitable form, for instance in the form of a hydrate, for instance cephalexin monohydrate.
  • Cefadroxil may be in any suitable form, for instance in the form of a hydrate, for instance cefadroxil monohydrate.
  • Cephradin may be in any suitable form, for instance in the form of a hydrate, for instance cephradin monohydrate.
  • Cefaclor may be in any suitable form, for instance in the form of a hydrate, for instance cefaclor monohydrate.
  • Amoxicillin may be in any suitable form, for instance in the form of a hydrate, for instance amoxicillin trihydrate.
  • Ampicillin may be in any suitable form, for instance in the form of a hydrate, for instance ampicillin trihydrate.
  • the ⁇ -lactam antiobiotic may be prepared in any suitable process known in the art, for instance using a chemical process or an enzymatic process.
  • cephalexin was prepared and recovered using the process as described in WO-A-9623796.
  • the cephalexin (monohydrate) crystals obtained were washed with water and subsequently with a water-acetone mixture containing 80 vol.% of acetone.
  • the resulting wet cake contained 8 wt.% of free water and 8 wt.% of acetone.
  • cephradine was prepared and recovered according to the method as described in WO 2005/003367, using PenG acylase mutant Phe-24-Ala.
  • the cephradine hydrate crystals obtained were washed with water and subsequently with a water-acetone mixture containing 80 vol.% of acetone.
  • the resulting wet cake contained 8 wt.% of free water and 8 wt.% of acetone.
  • the cephalexin wet cake was dried using a Vacuum Paddle dryer type SHV- 3000 supplied by Bachiller S. A., Spain.
  • the dryer was charged with 600 kg cephalexin wet cake produced as described above, containing 8 wt.% of free water and 8 wt.% of acetone.
  • the walls were heated at a temperature of 70 0 C (product temperature 40 0 C).
  • the final pressure was 20 mbar.
  • During drying the wet cake was stirred at a speed of 7 rpm. After 2 hours and 40 minutes of drying the product was discharged.
  • the water content was 5.2 wt.% (Karl Fisher).
  • the resulting powder having a temperature between 20-25 0 C, was fed to a roller compactor produced by Hosokawa-Bepex, type K200/100 operated at a roller speed of 12 rpm and a roller pressure of 130 kN.
  • the resulting compacted product was crushed to obtain granules having a bulk density above 0.45 g/ml and a tapped density above 0.75 g/ml.
  • the densities were determined using method Eur. Ph. 5.0, section 2.9.15 (with the difference that a 100 ml cylinder was used).
  • the resulting product was analysed for the H 2 S content using a HP 6890 gas chromatograph, and a Supelco SPB-1 sulfur, 30 m x 0.32 mm x 4.00 ⁇ m column.
  • 3 reference experiments were carried using gases containing known volume concentrations of H 2 S in N 2 : (0.5 vol ppm, 1.5 ppm, and 5.6 ppm). Using these reference experiments, a calibration curve was constructed.
  • the sample was equilibrated at ambient temperature (22 0 C) for 3 hours. After said 3 hours a sample of air (300 ⁇ l injection volume) from the vial was analysed.
  • the H 2 S vol ppm in said sample was 3.2 ppm.
  • the volume of the gas phase .above the sample was 14.5 ml (i.e. sample volume was 5.5 ml).
  • C H2 s( 3h) 11 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic.
  • This experiment was repeated 3 times, resulting in an average value for CH2s(3h) of 10 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic.
  • C H2 s(72h) of cephalexin granules from company A The CH 2 s(7 2h ) of cephalexin granules from company A was determined by weighing a sample of 3.5 to 4.5 g of the cephalexin granules into a vial of 20 ml. The H 2 S content was analysed as described above under ⁇ A.1., with the difference that the sample was equilibrated at an ambient temperature for 72 h. The average value for C H 2S(72b) of cephalexin granules from company A was 73 ⁇ l of H 2 S gas per kg of ⁇ - lactam antibiotic.
  • Comparative experiment A was repeated with the difference that the powder was cooled after drying.
  • a cooler (Vertical conical mixer, type MCV-3000-N, produced by Bachiller S. A.) was charged with 550 kg cephalexin powder. The wall temperature of the mixer was kept at a temperature of 5 0 C. The cephalexin was cooled in the cooler under mixing during 2 hours until a product temperature of just below 15 0 C was achieved.
  • the resulting powder was roller compacted as described above, and the C H2 s (3h) of the thus pepared cephalexin granules was determined. Due to the cooling the smell of the resulting product was significantly less intensive.
  • the C H2 S(7 2h ) of the cephalexin granules as prepared under ⁇ 1.1 was determined.
  • a sample of 3.5 to 4.5 g of the cephalexin granules was analysed for the H 2 S content according to the method as described under comparative experiment A.2., wherein the sample was equilibrated at ambient temperature (22 0 C) for 72 h.
  • the average value for C H2 s (72h ) was 21 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic.
  • the C H2 S(7 2h ) of cephradine granules from competitor B was determined.
  • the average value for CH2S(72 h ) of cephradine granules from competitor B was 28 ⁇ l of H 2 S gas per kg of ⁇ -lactam antibiotic.

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Abstract

The present invention relates to granules comprising a ß-lactam antibiotic, wherein CH2S(72h) < 50 µl of H2S gas per kg of β-lactam antibiotic, wherein CH2S(72h) is the volume of H2S gas above said granules per kg of said β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 °C during 72 hours at atmospheric pressure (1 bar). The invention also relates to a process for the preparation of granules comprising a ß-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the temperature of the β-lactam antibiotic that is fed to the roller compactor is sufficiently low that CH2S(72h) < 50 µl of H2S gas per kg of β-lactam antibiotic, wherein CH2S(72h) is the volume of H2S gas above said granules per kg of said β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 °C during 72 hours at atmospheric pressure (1 bar).

Description

GRANULES COMPRISING A β-LACTAM ANTIBIOTIC
The present invention relates to granules comprising a β-lactam antibiotic, to a process for the preparation thereof and to an apparatus for preparing the granules comprising the β-lactam antibiotic.
The preparation of a β-lactam antibiotic typically involves obtaining the β-lactam antibiotic as a crystalline powder, e.g. by crystallizing the β-lactam antibiotic from a solution, and drying the resulting crystals resulting in the powder. When improved physical properties are desired, e.g. bulk density or flowability, the powder may be compressed, e.g. by roller compacting to form granules comprising compressed powder. Roller compacting of a β-lactam antibiotic is e.g. described in WO-A-9911261.
It was found that the known process for the preparation of granules comprising a β-lactam antibiotic in compressed form results in a product having an unpleasant smell. It is an object of the invention to provide granules comprising having no smell or a smell that is at least less intensive.
This object is achieved by providing granules comprising a β-lactam antibiotic, wherein CH2S(72h) < 50 μl of H2S gas per kg of β-lactam antibiotic, wherein CH2S(72h) is the volume of H2S gas above said granules per kg of said β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar).
Preferably, the granules comprising a β-lactam antibiotic according to the invention, have a CH2s(72h) < 40 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(72h) < 30 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(72h) < 25 μl of H2S gas per kg of β-lactam antibiotic, preferably C^s^h) < 20 μl of H2S gas per kg of β- lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar). In an embodiment, the granules comprising a β-lactam antibiotic according to the invention have a CH2s(72h) > 1 μl of H2S gas per kg of β-lactam antibiotic. As used herein CH2S(72h) is determined under the following conditions: a sample of between 3.5 and 4.5 gram of said granules is kept in a closed container (volume of 20 ml) at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar). After said 72 hours a sample of air is taken from the container and analysed by gas chromatography to determine the volume fraction of H2S in said sample of air. Said volume fraction of H2S gas is multiplied by the gas phase volume above the sample (i.e. volume of the container, i.e. 20 ml, minus the volume of the sample) resulting in the volume of H2S gas in the container. The calculated value of said volume of H2S gas in the container is divided by the weight of the sample, resulting in CH2s(72h)- The invention also provides granules comprising a β-lactam antibiotic, wherein
CH2S(3h) < 10 μl of H2S gas per kg of β-lactam antibiotic, wherein CH2s(3h) is the volume of H2S gas above said granules per kg of said β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar). In the latter aspect of the invention, the CH2s(3h) is determined under the following conditions: a sample of between 3.5 and 4.5 gram of said granules is kept in a closed container (volume of 20 ml) at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar). After said 3 hours a sample of air is taken from the container and analysed by gas chromatography to determine the volume fraction of H2S in said sample of air. Said volume fraction of H2S gas is multiplied by the gas phase volume above the sample (i.e. volume of the container, i.e. 20 ml, minus the volume of the sample) resulting in the volume of H2S gas in the container. The calculated value of said volume of H2S gas in the container is divided by the weight of the sample, resulting in CH2S(3h). In a preferred embodiment, the invention provides granules comprising a β- lactam antibiotic, wherein CH2s(3h) < 9 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 8 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 7 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 6 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 5 μl of H2S gas per kg of β-lactam antibiotic when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar). In an embodiment, the granules comprising a β-lactam antibiotic according to the invention have a CH2s(3h) > 1 μl of H2S gas per kg of β-lactam antibiotic. Granules according to the invention may comprise auxiliaries or may be free of auxiliaries. Granules according to the invention may comprise compressed β-lactam antibiotic, for instance β-lactam antibiotic compressed by roller compacting. Granules according to the invention are preferably obtained by roller compacting. The granules according to the invention may for instance have a bulk density of between 0.4 and 1.0 g/ml, for instance between 0.45 and 0.8 g/ml. As used herein, bulk density is preferably determined using USP 24, method I, (page 1913). Preferably, bulk density is determined using method Eur. Ph. 5.0, section 2.9.15.
As auxiliaries may for instance be used fillers, dry binders, disintegrants, wetting agents, wet binders, lubricants, flow agents and the like. Examples of auxiliaries are lactose, starches, bentonite, calcium carbonate, mannitol, microcrystalline cellulose, polysorbate, sodium lauryl sulphate, carboxymethylcellulose Na, sodium alginate, magnesium stearate, silicon dioxid, talc. Preferably, the granules according to the invention are free of auxiliaries. The invention also provides a process for preparing granules according to the invention.
The invention provides a process for preparing granules comprising a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size- reducing, e.g. milling the compacts to produce granules, whereirtr the temperature of the β-lactam antibiotic that is fed to the roller compactor is sufficiently low that CH2s(72h) < 50 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s<72h) < 40 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(72h) < 30 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(72h) < 25 μl of H2S gas per kg of β-lactam antibiotic,preferably CH2S(72h) < 20 μl of H2S gas per kg of β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar).
In another embodiment, the invention provides a process for preparing granules comprising a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the temperature of the β-lactam antibiotic that is fed to the roller compactor is sufficiently low that CH2S(3h) < 10 μl of H2S gas per kg of β- lactam antibiotic, preferably CH2S(3h) < 9 μl of H2S gas per kg of β-lactam antibiotic, -A-
preferably Cπesβh) < 8 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2S(3h) < 7 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2S(3h) < 6 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h} < 5 μl of H2S gas per kg of β-lactam antibiotic when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar).
Surprisingly it was found that by cooling the antibiotic prior to feeding to the roller compactor decreases CH2s(72h) and CH2S(3II)-
In an embodiment, the invention provides a process for preparing granules comprising a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the said β-lactam antibiotic is cooled prior to said feeding.
In another embodiment, the invention provides a process for preparing granules comprising a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the temperature of the β-lactam antibiotic that is fed to said roller compactor is below 20 0C, preferably below 18 0C, more preferably bIlow 15 °C. The β-lactam antibiotic is preferably fed to the roller compactor as a crystalline powder of the β-lactam antibiotic, preferably without auxiliaries. However, it is also possible to feed a mixture comprising a crystalline powder and auxiliaries to the roller compactor.
As auxiliaries may for instance be used fillers, dry binders, disintegrants, wetting agents, wet binders, lubricants, flow agents and the like. Examples of auxiliaries are lactose, starches, bentonite, calcium carbonate, mannitol, microcrystalline cellulose, polysorbate, sodium lauryl sulphate, carboxymethylcellulose Na, sodium alginate, magnesium stearate, silicon dioxid, talc.
The roller compactor may be operated at any suitable roller pressure, for instance between 10 and 250 kN, for instance between 50-200 kN.
The invention also provides a β-lactam antibiotic in compressed form wherein CH2S(72h> < 50 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(72h) < 40 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(72h) < 30 μl of H2S gas per kg of β- lactam antibiotic, preferably CH2S(72h) < 25 μl of H2S gas per kg of β-lactam antibiotic preferably CH2s(72h) < 20 μl of H2S gas per kg of β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar). The invention also provides a β-lactam antibiotic in compressed form wherein
CH2S(3h) < 10 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2S(3h) < 9 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 8 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2S(3h) < 7 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2soh) < 6 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s@h) < 5 μl of H2S gas per kg of β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar). In an embodiment, the CH2s(3h) > 1 μl of H2S gas per kg of β-lactam antibiotic.
The invention also provides a process for compressing a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a step in which the β-lactam antibiotic is compressed to form compressed β-lactam antibiotic, wherein the temperature of the β-lactam antibiotic that is fed to said step is sufficiently low that CH2S(72h) < 50 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(72h) < 40 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2S(72h) < 30 μl of H2S gas per kg of β- lactam antibiotic, preferably CH2S(72h) < 25 μl of H2S gas per kg of β-lactam antibiotic,
CH2s(72h) < 20 μl of H2S gas per kg of β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar).
The invention also provides a process for compressing a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a step in which the β-lactam antibiotic is compressed to form compressed β-lactam antibiotic, wherein the temperature of the β-lactam antibiotic that is fed to said step is sufficiently low that CH2S(3II) < 10 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2S(3h> < 9 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 8 μl of H2S gas per kg of β-lactam antibiotic, CH2S(3h) < 7 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 6 μl of H2S gas per kg of β-lactam antibiotic, preferably CH2s(3h) < 5 μl of H2S gas per kg of β- lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar).
In an embodiment, the process comprises cooling the β-lactam antibiotic prior to said feeding. In an embodiment, the process comprises feeding said β-lactam antibiotic to a step in which the β-lactam antibiotic is compressed to form compressed β-lactam antibiotic, wherein the β-lactam antibiotic is cooled prior to said feeding.
In an embodiment, the temperature of the β-lactam antibiotic that is fed to said step is below 20 0C, preferably below 18 0C, more preferably below 15 0C. The invention also provides an apparatus comprising
(i) a cooler for cooling an antibiotic; and
(ii) a means for compressing the cooled antibiotic, wherein said (i) cooler is arranged such that the antibiotic can be cooled prior to feeding the antibiotic to (ii) the means for compressing the antibiotic, Preferably said means for compressing the antibiotic is a roller compactor.
Preferably, said apparatus further comprises a dryer for drying the β-lactam antibiotic, said dryer arranged such that the dried antibiotic can be fed to the cooler.
The β-lactam antibiotic is not limited to a specific type of β-lactam antibiotic. It may for instance be a penicillin, for instance ampicillin or amoxicillin, or a cephalosporin, for instance cephalexin, cefadroxil, cephradin, or cefalcor.
Cephalexin may be in any suitable form, for instance in the form of a hydrate, for instance cephalexin monohydrate.
Cefadroxil may be in any suitable form, for instance in the form of a hydrate, for instance cefadroxil monohydrate. Cephradin may be in any suitable form, for instance in the form of a hydrate, for instance cephradin monohydrate.
Cefaclor may be in any suitable form, for instance in the form of a hydrate, for instance cefaclor monohydrate.
Amoxicillin may be in any suitable form, for instance in the form of a hydrate, for instance amoxicillin trihydrate.
Ampicillin may be in any suitable form, for instance in the form of a hydrate, for instance ampicillin trihydrate. The β-lactam antiobiotic may be prepared in any suitable process known in the art, for instance using a chemical process or an enzymatic process.
EXAMPLES
Materials
In comparative experiment A and example 1 , cephalexin was prepared and recovered using the process as described in WO-A-9623796. The cephalexin (monohydrate) crystals obtained were washed with water and subsequently with a water-acetone mixture containing 80 vol.% of acetone. The resulting wet cake contained 8 wt.% of free water and 8 wt.% of acetone.
In addition one sample of cephalexin granules in comparative experiment A was obtained from company A.
In comparative experiment B, a sample of granules of cephradin was obtained from company B.
In example 2, cephradine was prepared and recovered according to the method as described in WO 2005/003367, using PenG acylase mutant Phe-24-Ala. The cephradine hydrate crystals obtained, were washed with water and subsequently with a water-acetone mixture containing 80 vol.% of acetone. The resulting wet cake contained 8 wt.% of free water and 8 wt.% of acetone.
Comparative experiment A
The cephalexin wet cake was dried using a Vacuum Paddle dryer type SHV- 3000 supplied by Bachiller S. A., Spain. The dryer was charged with 600 kg cephalexin wet cake produced as described above, containing 8 wt.% of free water and 8 wt.% of acetone. The walls were heated at a temperature of 70 0C (product temperature 40 0C). The final pressure was 20 mbar. During drying the wet cake was stirred at a speed of 7 rpm. After 2 hours and 40 minutes of drying the product was discharged. The water content was 5.2 wt.% (Karl Fisher). The resulting powder, having a temperature between 20-25 0C, was fed to a roller compactor produced by Hosokawa-Bepex, type K200/100 operated at a roller speed of 12 rpm and a roller pressure of 130 kN. The resulting compacted product was crushed to obtain granules having a bulk density above 0.45 g/ml and a tapped density above 0.75 g/ml. The densities were determined using method Eur. Ph. 5.0, section 2.9.15 (with the difference that a 100 ml cylinder was used).
The resulting product was analysed for the H2S content using a HP 6890 gas chromatograph, and a Supelco SPB-1 sulfur, 30 m x 0.32 mm x 4.00 μm column. 3 reference experiments were carried using gases containing known volume concentrations of H2S in N2: (0.5 vol ppm, 1.5 ppm, and 5.6 ppm). Using these reference experiments, a calibration curve was constructed.
A.1. Determination CH2s(3h) After this the CH2S(3h> of the cephalexin granules was determined.
A sample (4.04 gram), was introduced into a vial having a volume of 20 ml. The sample was equilibrated at ambient temperature (22 0C) for 3 hours. After said 3 hours a sample of air (300 μl injection volume) from the vial was analysed. The H2S vol ppm in said sample was 3.2 ppm. The volume of the gas phase .above the sample was 14.5 ml (i.e. sample volume was 5.5 ml). Hence, CH2s(3h) = 11 μl of H2S gas per kg of β-lactam antibiotic. This experiment was repeated 3 times, resulting in an average value for CH2s(3h) of 10 μl of H2S gas per kg of β-lactam antibiotic.
A.2. Determination CH2s(72h) of cephalexin granules from company A The CH2s(72h) of cephalexin granules from company A was determined by weighing a sample of 3.5 to 4.5 g of the cephalexin granules into a vial of 20 ml. The H2S content was analysed as described above under § A.1., with the difference that the sample was equilibrated at an ambient temperature for 72 h. The average value for CH2S(72b) of cephalexin granules from company A was 73 μl of H2S gas per kg of β- lactam antibiotic. Example 1
Comparative experiment A was repeated with the difference that the powder was cooled after drying.
A cooler (Vertical conical mixer, type MCV-3000-N, produced by Bachiller S. A.) was charged with 550 kg cephalexin powder. The wall temperature of the mixer was kept at a temperature of 5 0C. The cephalexin was cooled in the cooler under mixing during 2 hours until a product temperature of just below 15 0C was achieved.
1.1. Determination CH2s(3h)
The resulting powder was roller compacted as described above, and the CH2s(3h) of the thus pepared cephalexin granules was determined. Due to the cooling the smell of the resulting product was significantly less intensive.
1.2. Determination CH2S(72h)
In addition, the CH2S(72h) of the cephalexin granules as prepared under § 1.1 was determined. A sample of 3.5 to 4.5 g of the cephalexin granules was analysed for the H2S content according to the method as described under comparative experiment A.2., wherein the sample was equilibrated at ambient temperature (220C) for 72 h. The average value for CH2s(72h) was 21 μl of H2S gas per kg of β-lactam antibiotic.
Comparative experiment B
The CH2S(72h) of cephradine granules from competitor B was determined. A sample of 3.5 to 4.5 g of cephradine granules from competitor B was analysed for the H2S content according to the method as described under comparative experiment A, wherein the sample was equilibrated at ambient temperature for 72 h. The average value for CH2S(72h) of cephradine granules from competitor B was 28 μl of H2S gas per kg of β-lactam antibiotic. Example 2
The cephradine wet cake was dried and compacted according to the method as described under comparative experiment A with the difference that after drying the product was cooled as described in Example 1. Subsequently, the CH2s<72h) was determined as described under comparative experiment A.2. The average value for CH2S(72h) was 18 μl of H2S gas per kg of β-lactam antibiotic.
The results in Examples 1 to 2 show that cooling before compacting results in reduced concentrations of H2S.

Claims

5 1. Granules comprising a β-lactam antibiotic, wherein CH2s<72h) < 50 μl of H2S gas per kg of β-lactam antibiotic, wherein CH2s(72) is the volume of H2S gas above said granules per kg of said β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar). o
2. Granules according to claim 1 , wherein CH2S(72h) < 40 μl of H2S gas per kg of β-lactam antibiotic, preferably < 30 μl, more preferably < 25 μl of H2S gas per kg of β- lactam antibiotic.
3. Granules comprising a β-lactam antibiotic, wherein CH2s(3h) < 10 μl of H2S gas per kg of β-lactam antibiotic, wherein CH2s(3h) is the volume of H2S gas above said 5 granules per kg of said β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar).
4. Granules according to any one of the claims 1 to 3, said granules comprising compressed β-lactam antibiotic. o
5. Granules according to any one of the claims 1 to 4, wherein said granules comprise β-lactam antibiotic compressed by roller compacting.
6. Granules according to any one of the claims 1 to 5, wherein said granules are free of auxiliaries.
7. Granules according to any one of the claims 1 to 6 having a bulk density 5 of between 0.4 and 1.0 g/ml, for instance between 0.45 and 0.8 g/ml.
8. Granules according to any one of the claims 1 to 7, wherein said β-lactam antibiotic is a cephalosporin, preferably selected from the group consisting of cephalexin, cefadroxil, cephradin, and cefaclor.
9. Granules according to any one of the claims 1 to 7, wherein said β-lactam 0 antibiotic is a penicillin, preferably selected from the group consisting of amoxicillin and ampicillin.
10. Process for preparing granules comprising a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. milling the compacts to produce granules, wherein the temperature of the β-lactam antibiotic that is fed to the roller compactor is sufficiently low that CH2S(72) < 50 μl of H2S gas per kg of β-lactam antibiotic, wherein Chiasm is the volume of H2S gas above said granules per kg of said β-lactam antibiotic, when a 5 sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 72 hours at atmospheric pressure (1 bar).
11. Process for preparing granules comprising a β-lactam antibiotic, said process comprising feeding said β-lactam antibiotic to a roller compactor to form o compacts, size reducing, e.g. milling the compacts to produce granules, wherein the temperature of the β-lactam antibiotic that is fed to the roller compactor is sufficiently low that CH2s(3h) < 10 μl of H2S gas per kg of β-lactam antibiotic, when a sample of between 3.5 and 4.5 g of said granules is kept in a closed container having a volume of 20 ml at a temperature of 22 0C during 3 hours at atmospheric pressure (1 bar). 5
12. Process according to claim 10 or 11 , wherein the process comprises cooling the β-lactam antibiotic prior to said feeding.
13. Process for preparing granules comprising a β-lactam antibiotic, for instance according to any one of the claims 10 to 12, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. 0 milling the compacts to produce granules, wherein said β-lactam antibiotic is cooled prior to said feeding.
14. Process for preparing granules comprising a β-lactam antibiotic, for instance according to any one of the claims 10 to 13, said process comprising feeding said β-lactam antibiotic to a roller compactor to form compacts, size reducing, e.g. 5 milling the compacts to produce granules, wherein the temperature of the β-lactam antibiotic that is fed to said roller compactor is below 20 0C, preferably below 18 0C, more preferably below 15 0C.
15. Process according to any one of the claims 10 to 14, wherein said β- lactam antibiotic is a cephalosporin, preferably selected from the group consisting of o cephalexin, cefadroxil, cephradin and cefaclor.
16. Process according to any one of the claims 10 to 14, wherein said β- lactam antibiotic is a penicillin, preferably selected from the group consisiting of amoxicillin and ampicillin.
17. Granules obtainable by the process according to any one of the claims 11 to 16.
18. Apparatus comprising
(i) a cooler for cooling an β-lactam antibiotic; and (ii) a means for compressing the cooled antibiotic roller compactor, wherein the cooler is arranged such that the β-lactam antibiotic can be cooled prior to feeding the β-lactam antibiotic to the means for compressing the cooled β- lactam antibiotic.
19. Apparatus according to claim 18, wherein said apparatus further comprises a dryer for drying the β-lactam antibiotic, said dryer arranged such that the dried antibiotic can be fed to the cooler.
PCT/EP2005/053036 2004-06-30 2005-06-28 GRANULES COMPRISING A ß-LACTAM ANTIBIOTIC WO2006003152A1 (en)

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EP05756680.4A EP1786548B1 (en) 2004-06-30 2005-06-28 GRANULES COMPRISING A ß-LACTAM ANTIBIOTIC
BRPI0512933A BRPI0512933B8 (en) 2004-06-30 2005-06-28 roller compacted granules comprising (beta)-lactam antibiotic and process for preparing said granules
US12/889,307 US20110011961A1 (en) 2004-06-30 2010-09-23 Granules comprising a beta-lactam antibiotic

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US4134943A (en) * 1975-12-16 1979-01-16 Boehringer Mannheim Gmbh Production of porous tablets
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US6358526B1 (en) * 2000-08-16 2002-03-19 Rexall Sundown Method of making tablets and tablet compositions produced therefrom

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US3843639A (en) * 1973-02-08 1974-10-22 Bristol Myers Co Production of cephalexin via methoxymethyl ester
TWI225402B (en) * 1996-03-13 2004-12-21 Biochemie Gmbh Auxiliary-free agglomerates
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WO1999011261A1 (en) * 1997-08-29 1999-03-11 Dsm N.V. Granules free of excipients
US6358526B1 (en) * 2000-08-16 2002-03-19 Rexall Sundown Method of making tablets and tablet compositions produced therefrom

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