NO821174L - PROCEDURE FOR THE PREPARATION OF SODIUM AMOXILLIN - Google Patents

PROCEDURE FOR THE PREPARATION OF SODIUM AMOXILLIN

Info

Publication number
NO821174L
NO821174L NO821174A NO821174A NO821174L NO 821174 L NO821174 L NO 821174L NO 821174 A NO821174 A NO 821174A NO 821174 A NO821174 A NO 821174A NO 821174 L NO821174 L NO 821174L
Authority
NO
Norway
Prior art keywords
sodium
solution
procedure
preparation
amoxillin
Prior art date
Application number
NO821174A
Other languages
Norwegian (no)
Inventor
Joseph Herman Grossman
David Lee Warner
Original Assignee
Bristol Myers Co
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 Bristol Myers Co filed Critical Bristol Myers Co
Publication of NO821174L publication Critical patent/NO821174L/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D499/00Heterocyclic compounds containing 4-thia-1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. penicillins, penems; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulfur-containing hetero ring
    • C07D499/04Preparation
    • C07D499/14Preparation of salts
    • C07D499/16Preparation of salts of alkali or alkaline earth metals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D499/00Heterocyclic compounds containing 4-thia-1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. penicillins, penems; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulfur-containing hetero ring

Description

1 Foreliggende oppfinnelse vedrører fremstilling av fast natrium amoxicilian ved å sprøyte-tørke en løsning av natrium lam-' oxicillån i en blanding av vann og t-butanol. 1 The present invention relates to the production of solid sodium amoxicillin by spray-drying a solution of sodium lamoxicillan in a mixture of water and t-butanol.

Fast natrium amoxicillin har vært fremstilt ved utfellingSolid sodium amoxicillin has been prepared by precipitation

(som i UK 1,241.844 og UK 1. 286 .199) , men fra et kommersielt! . synspunkt er produktet funnet utilfredsstillende p.g.a. urenheter forårsaket av rester så som trietylamin eller natrium 2-etylhexanoat eller overskudd av løsningsmidler. (as in UK 1,241,844 and UK 1,286,199) , but from a commercial! . point of view, the product has been found unsatisfactory due to impurities caused by residues such as triethylamine or sodium 2-ethylhexanoate or excess solvents.

Fast natrium amoxicillin har også vært fremstilt ved fryse-tørking (UK 1.527,557.og UK 1.543.317), men dette forutsetter særdeles kostbart utstyr for å produsere tilstrekkelige mengder for salg; i tillegg kreves det meget lang produksjons-tid på grunn av de meget lave temperaturer som er nødvendige og som igjen reduserer produksjonsutstyrets effekt. Solid sodium amoxicillin has also been produced by freeze-drying (UK 1,527,557 and UK 1,543,317), but this requires extremely expensive equipment to produce sufficient quantities for sale; in addition, a very long production time is required due to the very low temperatures which are necessary and which in turn reduce the efficiency of the production equipment.

Ved fremgangsmåten ifølge foreliggende oppfinnelse benyttetIn the method according to the present invention used

man en sluttet syklussprøytetørker; hovedbestanddelere av dette apparat er tørkekammer, produkt-syklon, . avløpsvifte, kon-denser/renseanordning (støtplate, glykolavkjølt) nitrogenvifte, varmeveksler (Dowtherm) og matepumpe. Apparatet var konstruert for samvirkeoperasjon med syklonprodukt-avløpet. Enheten ble først spylet med nitrogen for å redusere oksygennivåst. til et sikkert nivå, slik at løsningsblandingen kunne føres til kon-denseren (dette muliggjør at konstante tørkebetingelser raskt oppnås.) Enheten fikk deretter den ønskede ^-innløpstemperatur, gasstrøm, kondensertemperatur etc. Matingen (natrium amoxicillin i vandig t-butanolløsning) ble pumpet gjennom en sprøyte-dyse på top-pen av tørkekammeret.. Tørketproduktet og gass ble ført gjennom bunnen for å bli separert i en syklon. one a closed cycle spray dryer; main components of this device are drying chamber, product cyclone, . drain fan, condenser/cleaning device (bumper plate, glycol-cooled) nitrogen fan, heat exchanger (Dowtherm) and feed pump. The device was designed for cooperative operation with the cyclone product drain. The unit was first flushed with nitrogen to reduce oxygen levels. to a safe level, so that the solution mixture could be fed to the condenser (this enables constant drying conditions to be quickly achieved.) The unit was then given the desired ^-inlet temperature, gas flow, condenser temperature, etc. The feed (sodium amoxicillin in aqueous t-butanol solution) was pumped through a spray nozzle on the top of the drying chamber. The dried product and gas were passed through the bottom to be separated in a cyclone.

Produkt data Product data

Bestemt på en vannfri løsningsfri basis ved anvendelse av British Pharmacopeia-fremgangsmåten for å måle forurensing av'penicillinsyre og dimere e.l. Determined on an anhydrous solution-free basis using the British Pharmacopeia method for measuring contamination by penicillinic acid and dimers, etc.

Renheten og de fysiske egenskapene til de fire produkteneThe purity and physical properties of the four products

av fast sprøytetørket natrium amoxicillin gjorde dem egnet for kommersielt bruk etter sterilisering med etylenoksyd. of solid spray-dried sodium amoxicillin made them suitable for commercial use after sterilization with ethylene oxide.

Under forberedelsen av innmatingen til tørkeren (oppløsnings-trinhet over) ble mikropulverisert amoxicillintrihydrat (aktivitet 845/ag/mg ) blandet i t-butanolløsning bestående av 2,4 1 vann og 1,5 1 t-butanol pr. kg amoxicillin trihydrat ved 25°C. Til denne suspensjon ble tilsatt 1,97N vandig natrium-hydroksyd kontinuerlig til et overskudd på -,:a. 2% (1,23 l/kg) . During the preparation of the feed to the dryer (solution step above), micropulverized amoxicillin trihydrate (activity 845/ag/mg) was mixed in t-butanol solution consisting of 2.4 1 water and 1.5 1 t-butanol per kg amoxicillin trihydrate at 25°C. To this suspension was added 1.97N aqueous sodium hydroxide continuously to an excess of -,:a. 2% (1.23 l/kg) .

Tørke; trinn Produktresultater ^ Bestemt på en vannfri oppløsningsfri bas. ved anvendelse av British Pharmacopeia for å måle forurensning av penicillinsyre og dimere e.l. Tørketrinn -Produkt re sul ta ter Drought; step Product results ^ Determined on an anhydrous solvent-free basis using the British Pharmacopeia to measure contamination of penicillin acid and dimers etc. Drying step - Product results

Bestemt på en vannfri løsningsfri basis ved anvendelse av British Pharmacopeia-fremgangsmåten for å måle forurensning av penicillinsyrebg dimere e.l. Determined on an anhydrous solution-free basis using the British Pharmacopeia method for measuring contamination by penicillin acid bg dimers, etc.

Ved sprøytetørke-trinnet blir trykket variert for å oppnå den ønskede partikkelstørrelse. In the spray drying step, the pressure is varied to achieve the desired particle size.

Anvendelse av sprøytetørke-fremgangsmåten under sterile forhold ved å benytte " trykkdyse .. for å produsere steriltfast natrium amoxicillin gjør at man kan.fylle stoffet direkte i ampuller under sterile forhold.. Application of the spray-drying method under sterile conditions by using a "pressure nozzle .. to produce sterile solid sodium amoxicillin allows one to fill the substance directly into ampoules under sterile conditions..

De antibakterielle egenskaper og kliniske metoder ved bruk av amoxicillin er velkjente i medisinsk litteratur når det gjelder den orale anvendelse av. dets trihydrat. Ved parenteral admini-strering er det ofte foretrukket å injisere en vandig løsning som krever omdannelse av det uoppløslige trihydrat til et meget oppløselig •■ natriumsalt ifølge fremgangsmåten ved foreliggende oppfinnelse. Resultatene av den parenterale aministrering av vandig natrium amoxicillin er beskrevet f.eks. av D. A. Spyker et al., Pharmacokinetics of amoxycillin: "Dose dependence after intravenous, oral and intramuscular admini-stration"; Antimicrobial Agents and Chemotherapy, . 11, 132 The antibacterial properties and clinical methods of using amoxicillin are well known in the medical literature when it comes to the oral application of. its trihydrate. For parenteral administration, it is often preferred to inject an aqueous solution which requires conversion of the insoluble trihydrate into a highly soluble sodium salt according to the method of the present invention. The results of the parenteral administration of aqueous sodium amoxicillin are described e.g. by D. A. Spyker et al., Pharmacokinetics of amoxycillin: "Dose dependence after intravenous, oral and intramuscular administration"; Antimicrobial Agents and Chemotherapy, . 11, 132

(1977) and by-S.A. Hill et al., "Pharmacokinetics of parenter-ally administered amoxycillin", Journal of Infection 2, 320-332 (1980). (1977) and by-S.A. Hill et al., "Pharmacokinetics of parenterally administered amoxycillin", Journal of Infection 2, 320-332 (1980).

Claims (3)

1 . ''Fremgangsmåte ved fremstilling av fast natrium amoxicillin karakterisert ved å sprøyte-tørke en oppløsning av natrium amoxicillin i vandig t-butanoloppløsning..1. "Procedure for the production of solid sodium amoxicillin characterized by spray-drying a solution of sodium amoxicillin in aqueous t-butanol solution. 2. Fremgangsmåte ifølge krav 1, karakter i— sert védat innløpstemperaturen er ca. 180°C og utløpstemperaturen ca. 120°C.2. Method according to claim 1, grade i— ensured that the inlet temperature is approx. 180°C and the outlet temperature approx. 120°C. 3. Fremgangsmåte ifølge krav 1, karakterisert ved at oppløsningen som sprøytetørkes inneholder 1,5 1 t-butanol for hver 3,6 1 vann.3. Method according to claim 1, characterized in that the solution which is spray-dried contains 1.5 1 t-butanol for every 3.6 1 water.
NO821174A 1981-04-10 1982-04-06 PROCEDURE FOR THE PREPARATION OF SODIUM AMOXILLIN NO821174L (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR8107247A FR2503710B1 (en) 1981-04-10 1981-04-10 PROCESS FOR PRODUCING SODIUM SALT OF AMOXICILLIN

Publications (1)

Publication Number Publication Date
NO821174L true NO821174L (en) 1982-10-11

Family

ID=9257255

Family Applications (1)

Application Number Title Priority Date Filing Date
NO821174A NO821174L (en) 1981-04-10 1982-04-06 PROCEDURE FOR THE PREPARATION OF SODIUM AMOXILLIN

Country Status (23)

Country Link
JP (1) JPS57179191A (en)
KR (1) KR880001410B1 (en)
AU (1) AU559766B2 (en)
BE (1) BE892451A (en)
CA (1) CA1182108A (en)
CH (1) CH651836A5 (en)
DE (1) DE3213308A1 (en)
DK (1) DK157382A (en)
ES (1) ES511295A0 (en)
FI (1) FI821247L (en)
FR (1) FR2503710B1 (en)
GB (1) GB2096599B (en)
GR (1) GR76106B (en)
IE (1) IE52939B1 (en)
IT (1) IT1148165B (en)
LU (1) LU84007A1 (en)
NL (1) NL8201467A (en)
NO (1) NO821174L (en)
NZ (1) NZ200281A (en)
PT (1) PT74727B (en)
SE (1) SE8202269L (en)
YU (1) YU43132B (en)
ZA (1) ZA822400B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0131147B2 (en) * 1983-06-10 1996-12-04 Beecham Group p.l.c. Crystalline amoxycillin salt
IT1255716B (en) * 1992-10-05 1995-11-10 PROCEDURE FOR THE PREPARATION OF STERILE BETA-LACTAMIC ANTIBIOTICS
AT412213B (en) * 2000-05-30 2004-11-25 Sandoz Ag METHOD FOR DRYING AMOXICILLIN OR AMOXICILLIN-CONTAINING, ORAL, SOLID PHARMACEUTICAL COMPOSITIONS USING A GAS WITH A DEFINED GAS HUMIDITY
CN105055169B (en) * 2015-07-11 2019-01-22 鲁南制药集团股份有限公司 A method of preparing Imipenem and Cilasatin Sodium aseptic powdery

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1471235A (en) * 1974-09-18 1977-04-21 Beecham Group Ltd Amoxycillin derivatives
GB1527557A (en) * 1976-07-07 1978-10-04 Beecham Group Ltd Process for preparing solid sodium amoxycillin
GB1576731A (en) * 1976-08-10 1980-10-15 Beecham Group Ltd Process for the preparation of sodium amoxycillin
EP0012496B1 (en) * 1978-12-08 1983-07-20 Beecham Group Plc A process for the preparation of a solid sodium amoxycillin and aqueous solutions thereof

Also Published As

Publication number Publication date
KR880001410B1 (en) 1988-08-01
YU43132B (en) 1989-04-30
IT8248188A0 (en) 1982-04-07
IT1148165B (en) 1986-11-26
GB2096599A (en) 1982-10-20
PT74727A (en) 1982-05-01
NZ200281A (en) 1984-12-14
DE3213308A1 (en) 1982-11-11
IE820844L (en) 1983-10-10
ES8304138A1 (en) 1983-02-16
DK157382A (en) 1982-10-11
SE8202269L (en) 1982-10-11
FR2503710A1 (en) 1982-10-15
GB2096599B (en) 1985-01-23
FR2503710B1 (en) 1985-07-05
PT74727B (en) 1985-01-08
FI821247L (en) 1982-10-11
LU84007A1 (en) 1983-02-22
NL8201467A (en) 1982-11-01
ZA822400B (en) 1983-02-23
FI821247A0 (en) 1982-04-07
JPS57179191A (en) 1982-11-04
AU559766B2 (en) 1987-03-19
YU43282A (en) 1985-06-30
AU8045582A (en) 1982-10-14
IE52939B1 (en) 1988-04-13
CH651836A5 (en) 1985-10-15
ES511295A0 (en) 1983-02-16
CA1182108A (en) 1985-02-05
GR76106B (en) 1984-08-03
BE892451A (en) 1982-09-10
JPH0219119B2 (en) 1990-04-27
KR830010116A (en) 1983-12-26

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