DK143030B - PROCEDURE FOR IN-SITU PREPARATION OF A CEPHALOSPORIN C DERIVATE - Google Patents

PROCEDURE FOR IN-SITU PREPARATION OF A CEPHALOSPORIN C DERIVATE Download PDF

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DK143030B
DK143030B DK352569A DK352569A DK143030B DK 143030 B DK143030 B DK 143030B DK 352569 A DK352569 A DK 352569A DK 352569 A DK352569 A DK 352569A DK 143030 B DK143030 B DK 143030B
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cephalosporin
formula
acid
aca
preparation
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DK352569A
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DK143030C (en
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D A Johnson
E J Richardson
J M K Roubie
H H Silvestri
R R Smith
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Bristol Myers Co
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/02Silicon compounds
    • C07F7/08Compounds having one or more C—Si linkages
    • C07F7/18Compounds having one or more C—Si linkages as well as one or more C—O—Si linkages
    • C07F7/1896Compounds having one or more Si-O-acyl linkages

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  • Organic Chemistry (AREA)
  • Cephalosporin Compounds (AREA)

Description

1 1430301 143030

Den foreliggende opfindelse angår en fremgangsmåde til in situ fremstilling af et cephalosporin C-derivat med den almene formel H OH c I ·» I y/0 13 HO~C-C- (CH0 ) -j-C-N--f 1 l y Å i oThe present invention relates to a process for in situ preparation of a cephalosporin C derivative of the general formula H OH c I · I γ / 0 13 HO C C-C- (CHO) -j-C-N - f

NH .. IIINH .. III

' n -CH~-0-C-CH, c=° ^2 3a -CH ~ -0-C-CH, c = ° ^ 2 3

B ° IB ° I

co2h hvor B betegner en gruppe med formlen -NBR eller -OR, idet R betegner alkyl med 1-10 carbonatomer eller en gruppe med formlen 2 143030 hvor n betegner et helt tal fra 1 til 6, når B betegner OR, og fra 2 3 0 til 6, når B betegner NHR, og R og R er ens eller forskellige og betegner hver H, Cl, Br, F, NOg, alkyl indeholdende 1-10 carbon-atomer eller alkoxy indeholdende 1-10 carbonatomer. Dette derivat kan anvendes til fremstilling af 7-aminocephalosporansyre (7-ACA).co2h where B represents a group of formula -NBR or -OR, where R represents alkyl of 1-10 carbon atoms or a group of formula 2 where n represents an integer from 1 to 6 when B represents OR and from 2 to 3 0 to 6 when B represents NHR and R and R are the same or different and each represents H, Cl, Br, F, NOg, alkyl containing 1-10 carbon atoms or alkoxy containing 1-10 carbon atoms. This derivative can be used to prepare 7-aminocephalosporanoic acid (7-ACA).

Metoder til udvinding af cephalosporin C fra et dyrkningsmedium er omhandlet i beskrivelserne til USA-patenter nr. 3.093.638 og 3.094.527, hvor cephalosporin C adsorberes på en adsorbant i stedet for ekstraktion ved hjælp af et opløsningsmiddel. Mens lavere alkoxy-carbonyl- eller aryloxycarbonyl- eller (lavere)aikyicarbamoyl- eller arylcarbamoyl-cephalosporin C-derivater ikke er beskrevet som dannet "in situ" i cephalosporin C-dyrkningsmediet, eller som anvendelige ved ekstraktion af cephalosporin C fra næringsmediet eller som anvendelige som udgangsmaterialer til fremstilling af 7-ACA, er nogle af disse forbindelser beskrevet i patentlitteraturen (britiske patenter nr.Methods for recovering cephalosporin C from a culture medium are disclosed in the disclosures of U.S. Patents Nos. 3,093,638 and 3,094,527, wherein cephalosporin C is adsorbed on an adsorbent instead of solvent extraction. While lower alkoxy-carbonyl or aryloxycarbonyl or (lower) alycarbamoyl or arylcarbamoyl-cephalosporin C derivatives are not described as being formed "in situ" in the cephalosporin C culture medium, or as useful in extracting cephalosporin C from the nutrient medium or as useful as starting materials for the preparation of 7-ACA, some of these compounds are described in the patent literature (British Patent Nos.

1.014.883 og 1.064.495 samt USA-patenterne nr. 3.227.709 og 3.227.712 som antibiotika). Adskillige fremgangsmåder til kemisk spaltning af cephalosporin C eller visse af dets derivater er beskrevet i patentlitteraturen (USA-patenter nr. 1.188.311, 3.234.223 og 3.124.576 samt britisk patent nr. 1.041.985). Ingen af disse fremgangsmåder anvender N-(lavere)alkyloxycarbonyl- eller N-(lavere)alkyl- eller arylcarbamoylcephalosporin C og en silylester deraf som udgangsmateriale.1,014,883 and 1,064,495 as well as U.S. Patents Nos. 3,227,709 and 3,227,712 as antibiotics). Several methods of chemically cleaving cephalosporin C or some of its derivatives are described in the patent literature (U.S. Patents Nos. 1,188,311, 3,234,223 and 3,124,576, and British Patent Nos. 1,041,985). None of these processes use N- (lower) alkyloxycarbonyl or N- (lower) alkyl or arylcarbamoylcephalosporin C and a silyl ester thereof as starting material.

7-aminocephalosporansyre (7-ACA), der har formlen II7-aminocephalosporanoic acid (7-ACA) having the formula II

0 „_N J_CH9-0-'C-CH, 2 30 "_N J_CH9-0 -'C-CH, 2 3

C02H IICOH 2 II

er et yderst værdifuldt mellemprodukt ved fremstillingen af et stort antal semi-syntetiske, antibakterielle cephalosporansyrederivater. På grund af vanskelighederne ved en total syntese af 7-ACA i stor måle- 3 143030 stok fremstilles denne forbindelse I praksis ved kemisk nedbrydning af naturligt forekommende cephalosporansyre, dvs. cephalosporin C, der fremstilles ved fermentering. Det meste 7-ACA fremstilles således af cephalosporin C (USA-patent nr. 3.093.638), der har formlen 05 ? S H .S.is an extremely valuable intermediate in the preparation of a large number of semi-synthetic antibacterial cephalosporanoic acid derivatives. Due to the difficulties of total synthesis of 7-ACA on a large scale, this compound is prepared in practice by the chemical degradation of naturally occurring cephalosporanoic acid, ie. cephalosporin C produced by fermentation. Thus, most 7-ACA is made from cephalosporin C (U.S. Patent No. 3,093,638) having the formula 05? S H .S.

h2n - c - (ch2)3 - C - N X \ COzH o 10 i--012 ' 0 ' C ' “3h2n - c - (ch2) 3 - C - N X \ COzH o 10 i - 012 '0' C '“3

°X I° X I

C02H 1 15CO 2 H 1 15

Fremstillingen af 7-ACA ved de metoder, som idag er tilgængelige, er imidlertid fyldt med vanskeligheder lige fra gæringen til den kemiske spaltning af cephalosporin C. Lave udbytter af 7-ACA har således 20 gjort det vanskeligt for cephalosporansyrer at indtage den disse tilkommende plads inden for den antibiotiske terapi.However, the preparation of 7-ACA by the methods available today is fraught with difficulties ranging from the fermentation to the chemical decomposition of cephalosporin C. Thus, low yields of 7-ACA have made it difficult for cephalosporanoic acids to occupy this additional space. in the field of antibiotic therapy.

Cephalosporin C er karakteriseret ved en aminosyrefunktion i sidekæden. Aminosyren eksisterer i form af en zwitterion i vandig opløsning, og som sådan er den meget vandopløselig. Pi grund af 25 dens stærkt ioniske karakter er den yderst vanskelig at udvinde ved ekstraktion med opløsningsmiddel fra dyrkningsmediet. Udvindingsmetoden, som idag anvendes, omfatter adsorption af det rå cephalosporin C fra dyrkningsmediet på en passende adsorbant, f.eks. trækul, en ionbytterharpiks eller tilsvarende efterfulgt af eluering, 30 koncentrering og udfældning ved det isoelektriske punkt eller ved saltdannelse (USA-patent nr. 3.094.527). Den lave effektivitetsgrad i forbindelse med kompleksiteten for hvert trin ved denne fremgangsmåde gør det alt i alt meget vanskeligt at fremstille 7-ACA.Cephalosporin C is characterized by an amino acid function in the side chain. The amino acid exists in the form of a zwitterion in aqueous solution and as such it is highly water soluble. Due to its highly ionic nature, it is extremely difficult to recover by solvent extraction from the culture medium. The recovery method used today involves adsorption of the crude cephalosporin C from the culture medium onto a suitable adsorbent, e.g. charcoal, an ion exchange resin or the like, followed by elution, concentration and precipitation at the isoelectric point or by salt formation (U.S. Patent No. 3,094,527). The low efficiency of the complexity of each step of this process makes it very difficult to prepare 7-ACA.

Det er endvidere kendt at fremstille 7-ACA ved partiel nedbryd-35 ning af derivater af cephalosporin C ved kemiske midler (USA-patenter nr. 3.124.576, 3.188.311 og 3.234.223). Igen gælder det, at disse metoder giver praktiske udbytter, som er uønskeligt lave. Endvidere 4 143030 må disse metoder uundgåeligt som udgangsmateriale anvende en renset form af cephalosporin C, som er vanskelig at opnå.Further, it is known to prepare 7-ACA by partial degradation of derivatives of cephalosporin C by chemical agents (U.S. Patents Nos. 3,124,576, 3,188,311 and 3,234,223). Again, these methods provide practical yields that are undesirably low. Furthermore, these methods must inevitably use as a starting material a purified form of cephalosporin C which is difficult to obtain.

Det har nu uventet vist sig, at det ved fremgangsmåden ifølge opfindelsen in situ fremstillede cephalosporin C-derivat (III) uden 05 væsentlige rensningstrin direkte kan anvendes i efterfølgende spaltningsreaktioner til frembringelse af 7-ACA.It has now unexpectedly been found that the in situ process of the cephalosporin C derivative (III) prepared in situ without 05 significant purification steps can be used directly in subsequent cleavage reactions to produce 7-ACA.

Fremgangsmåden ifølge opfindelsen til in situ fremstilling af cephalosporin C-derivatet (III) er ejendommelig ved, at man sætter et acyleringsmiddel i form af et isocyanat med formlen 10 R - N = C = OThe process of the invention for in situ preparation of the cephalosporin C derivative (III) is characterized by the addition of an acylating agent in the form of an isocyanate of the formula 10 R - N = C = O

eller et halogenformiat med formlenor a halogen formate of the formula

OISLAND

IIII

X - C - O - RX - C - O - R

15 hvor R har den ovenfor anførte betydning, og X betegner chlor, brom eller iod, til et syre-inkuberet dyrkningsmedium indeholdende cephalosporin C, i et forhold på mindst 2 mol acyleringsmiddel pr. mol cephalosporin C ved en pH-værdi over 7 ved en temperatur under 40°C til dannelse af nævnte derivat af cephalosporin C.Wherein R is as defined above, and X represents chlorine, bromine or iodine, to an acid-incubated culture medium containing cephalosporin C, at a ratio of at least 2 moles of acylating agent per liter. mole of cephalosporin C at a pH above 7 at a temperature below 40 ° C to form said derivative of cephalosporin C.

20 Til opnåelse af de størst mulige udbytter og færrest mulige bi produkter foretrækkes de i krav 2-6 angivne foranstaltninger.20 In order to achieve the highest possible yields and the fewest possible by-products, the measures specified in claims 2-6 are preferred.

Dyrkning af den som skimmelsvamp kendte cephalosponum eller en mutant heraf giver en blanding af forbindelser, fortrinsvis cephalosporin C og mindre mængder cephalosporin N (der nu vides at være 25 penicillin). Cephalosporin C er syrestabil, mens cephalosporin N ikke er det. Som følge deraf foretrækkes det inden omsætningen af dyrkningsmediet med et halogenformiat at ødelægge in situ eventuelt samtidigt fremstillet cephalosporin N. Dette sker ved, at der gøres sur til en pH-værdi på ca. 2 med en mineralsyre, såsom saltsyre, svovl-30 syre, phosphorsyre eller lignende, efterfulgt af en inkuberingsperi-ode fra 2 til 10 timer. Dyrkningssubstratet kan filtreres før eller efter der gøres sur og inkuberes.Cultivation of the mold known cephalosponum or a mutant thereof produces a mixture of compounds, preferably cephalosporin C and smaller amounts of cephalosporin N (now known to be 25 penicillin). Cephalosporin C is acid stable, while cephalosporin N is not. As a result, prior to reacting the culture medium with a halogen formate, it is preferable to destroy in situ possibly co-produced cephalosporin N. This is achieved by acidifying it to a pH of approx. 2 with a mineral acid such as hydrochloric acid, sulfuric acid, phosphoric acid or the like, followed by an incubation period of from 2 to 10 hours. The culture substrate can be filtered before or after acidification and incubation.

Efter dette trin indstilles filtrat-dyrkningssubstratet indeholdende cephalosporin C til en pH-værdi fra 7 til 9, fortrinsvis ca. 8, 35 ved tilsætning af en alkalimetal base, såsom kalium- eller natriumhydroxid.After this step, the filtrate culture substrate containing cephalosporin C is adjusted to a pH of 7 to 9, preferably about 8, 35 by the addition of an alkali metal base such as potassium or sodium hydroxide.

5 1430305 143030

Voluminet af det fremstillede substrat øges til ca. 25% ved tilsætning af et forhold på mindst 2, fortrinsvis fra 2 til 10 mol acyle-ringsmiddel pr. mol cephalosporin C (idet substratkoncentrationen på forhånd er blevet bestemt) og særlig foretrukket i et forhold fra 05 5 til 8 mol. pH-værdien holdes konstant under den langsomme tilsæt ning og i mindst 30 minutter efter tilsætningen. Substratets temperatur holdes under 40°C, fortrinsvis ved 0-15°C i dette tidsrum. Omsætningen er sædvanligvis afsluttet en time efter, at tilsætningen er færdig.The volume of the substrate produced is increased to approx. 25% by adding a ratio of at least 2, preferably from 2 to 10 moles of acylating agent per minute. mole of cephalosporin C (with the substrate concentration predetermined) and particularly preferred in a ratio of 05 to 8 moles. The pH is kept constant during the slow addition and for at least 30 minutes after the addition. The temperature of the substrate is kept below 40 ° C, preferably at 0-15 ° C during this time. The turnover is usually completed one hour after the addition is complete.

10 Fortrinsvis tilsættes et halvt volumen af et ikke blandbart orga nisk opløsningsmiddel, fortrinsvis methylisobutylketon (MIBK), nlr acyleringsmidlet er et halogenformiat, og n-butanol, når acyleringsmid-let er et isocyanat, og pH-værdien indstilles til fra 1 til 3, fortrinsvis 2. Blandingen omrøres, og den organiske opløsningsmiddelfase inde-15 holdende cephalosporin C-derivat III opsamles.Preferably, half a volume of an immiscible organic solvent, preferably methyl isobutyl ketone (MIBK), is added, when the acylating agent is a halogen formate and n-butanol when the acylating agent is an isocyanate and the pH is adjusted to from 1 to 3. preferably 2. The mixture is stirred and the organic solvent phase containing cephalosporin C derivative III is collected.

Den organiske opløsning koncentreres i vakuum til ca. 1/3 af dens oprindelige volumen ved en temperatur, der ikke overstiger 40°C. Koncentratet afkøles til ca. 20°C til 30°C, og natriumsaltet af cephalosporinderivat III udfældes ved tilsætning af et ringe overskud 20 af natrium 2-ethylhexanoat opløst i et opløsningsmiddel, såsom MIBK eller n-butanol. Blandingen afkøles til 0-5°C i 3-4 timer, og det faste natriumsalt af derivat III opsamles ved filtrering. Filterkagen vaskes med kold MIBK efterfulgt af en udvaskning med n-hexan. Produktet tørres i vakuum ved ca. 25°C.The organic solution is concentrated in vacuo to ca. 1/3 of its original volume at a temperature not exceeding 40 ° C. The concentrate is cooled to approx. 20 ° C to 30 ° C and the sodium salt of cephalosporin derivative III is precipitated by the addition of a small excess 20 of sodium 2-ethylhexanoate dissolved in a solvent such as MIBK or n-butanol. The mixture is cooled to 0-5 ° C for 3-4 hours and the solid sodium salt of derivative III is collected by filtration. The filter cake is washed with cold MIBK followed by a washout with n-hexane. The product is dried in vacuo at ca. 25 ° C.

25 Forbindelserne med formlen III eller metal- eller aminsalte deraf kan uden nødvendigheden af forudgående rensning eller kemisk omdannelse til cephalosporin C anvendes til fremstilling af 7-ACA.The compounds of formula III or metal or amine salts thereof can be used to prepare 7-ACA without the need for prior purification or chemical conversion to cephalosporin C.

Dette kan ske ved en fremgangsmåde, som i det væsentlige består i følgende konsekutive trin: 6 143030 (A) blanding af en forbindelse med formlen H OH -This can be accomplished by a process which essentially consists of the following consecutive steps: mixing a compound of formula H OH -

M0?C-C-(CH9U-C-N --f NM0? C-C- (CH9U-C-N --f N

L ’ 0 05 NHL '0 05 NH

' >- . -CH--0-C-CH, c=o of L 3'> -. -CH - 0-C-CH, c = o or L 3

B C02MB C02M

10 hvor B betegner -OR eller -NHR, M betegner hydrogen, metal- eller aminkationer, og R betegner (lavere)alkyl, fortrinsvis ethyl, n-propyl, isopropyl, n-butyl og isobutyl eller en aralkylgruppe med formlen /-^r2 15 -(‘H2)n-f $3 2 3 hvor n betegner et helt tal fra 1 til 6, og R og R er ens eller 20 forskellige, og hver betegner H, Cl, Br, F, NC^, (lavere)alkyl eller (lavere)alkoxy, fortrinsvis hydrogen, med mindst to ækvivalenter af en silylforbindelse med formlen r* • 25 λ R5 „ NH /NH Λ 6 ·Wherein B represents -OR or -NHR, M represents hydrogen, metal or amine cations, and R represents (lower) alkyl, preferably ethyl, n-propyl, isopropyl, n-butyl and isobutyl or an aralkyl group of the formula 15 - ('H2) nf $ 3 2 3 where n represents an integer from 1 to 6, and R and R are the same or 20 different and each represents H, Cl, Br, F, NC (lower) alkoxy, preferably hydrogen, having at least two equivalents of a silyl compound of the formula r * • 25 λ R5 NH NH / NH Λ 6 ·

r4 i / | r4 eller R -Si_Xr4 i / | r4 or R -Si_X

^Si SC R^ Si SC R

,·/ yy., · / Yy.

30 IV \ ’ 5 6 7 hvor R , R og R betegner hydrogen, halogen, (lavere)alkyl, halo-Wherein R, R and R are hydrogen, halogen, (lower) alkyl, halo,

C CC C

gen (lavere)alkyl eller phenyl, idet mindst en af grupperne R , Rgene (lower) alkyl or phenyl, with at least one of the groups R, R

7 4 og R er forskellige fra halogen eller hydrogen, R betegner (lave- 35 re)alkyl, m er et helt tal pi 1-2, og X betegner halogen eller gruppen 143030 7 R8 κ7 4 and R are different from halogen or hydrogen, R represents (lower) alkyl, m is an integer p1 1-2 and X represents halogen or the group R8 κ

-N-N

\9 8 9 hvor R betegner hydrogen eller (lavere)alkyl, og R betegner hy- 05 drogen (lavere)alkyl eller gruppen R5 .Wherein R represents hydrogen or (lower) alkyl and R represents hydrogen (lower) alkyl or the group R5.

R6— Si — k7 fortrinsvis dimethyldichlorsilan eller trimethylchlorsilan, under vand- 10 fri betingelser i nærværelse af en syredeaktiverende tertiær amin, der kan være triethylamin, dimethylanilin, quinolin, lutidin eller py-ridin, i et inert opløsningsmiddel, der kan være methylenchlorid, dichlorethan, chloroform, tetrachlorethan, nitromethan eller diethyl-ether, til frembringelse af den tilsvarende silyl di-ester af forbind- 15 elsen III, (B) blanding af silyl di-esteren med et halogeneringsmiddel, der kan være phosphorpentachlorid, phosphorpentabromid, phosphor-trichlorid, phosphortribromid, oxalylchlorid, p-toluensulfonylhaløgenid, phosphoroxychlorid, phosgen eller lignende, i et molært forhold på 20 2 eller flere mol halogeneringsmiddel pr. mol silylester, fortrinsvis ca. 2 mol, under vandfri betingelser i et inert opløsningsmiddel, såsom methylenchlorid, dichlorethan, chloroform, tetrachlorethan, nitromethan, diethylether eller lignende i nærværelse af en syredeaktiverende tertiær amin, i form af triethylamin, diethylanilin, 25 quinolin, lutidin, pyridin eller lignende ved temperaturer under 0°C, fortrinsvis i intervallet fra 40°C til -60°C, til frembringelse i opløsning af det tilsvarende imino-halogenid, (C) blanding af nævnte opløsning af imino-halogenid med en alkohol i form af alifatiske alkoholer, indeholdende 1-12 carbonatomer 30 eller phenylalkylalkoholer, indeholdende 1-7 carbonatomer ved en temperatur under 0°C, fortrinsvis -40°C til -70°C, til frembringelse i opløsning af den tilsvarende iminoether samt (D) blanding af nævnte opløsning af imino-ether under sure betingelser med vand eller en alkohol, især en alifatisk alkohol eller 35 en blanding af begge til frembringelse af 7-amlnocephalosporansyre.R 6 - Si - k 7 preferably dimethyl dichlorosilane or trimethyl chlorosilane, under anhydrous conditions in the presence of an acid deactivating tertiary amine which may be triethylamine, dimethylaniline, quinoline, lutidine or pyridine, in an inert solvent which may be methylene chloride, d. , chloroform, tetrachloroethane, nitromethane or diethyl ether, to give the corresponding silyl diester of compound III, (B) mixing the silyl diester with a halogenating agent which may be phosphorus pentachloride, phosphorus pentabromide, phosphorus trichloride phosphorus tribromide, oxalyl chloride, p-toluenesulfonyl halogenide, phosphorus oxychloride, phosgene or the like, in a molar ratio of 20 or more moles of halogenating agent per moles of silyl ester, preferably ca. 2 mol, under anhydrous conditions in an inert solvent such as methylene chloride, dichloroethane, chloroform, tetrachloroethane, nitromethane, diethyl ether or the like in the presence of an acid deactivating tertiary amine in the form of triethylamine, diethylaniline, quinoline, lutidine, pyridine or the like. below 0 ° C, preferably in the range of 40 ° C to -60 ° C, to produce in solution of the corresponding imino halide, (C) mixing said solution of imino halide with an alcohol in the form of aliphatic alcohols containing 1-12 carbon atoms or phenylalkyl alcohols containing 1-7 carbon atoms at a temperature below 0 ° C, preferably -40 ° C to -70 ° C, to produce in solution of the corresponding imino ether and (D) mixing said solution of imino -ether under acidic conditions with water or an alcohol, especially an aliphatic alcohol or a mixture of both to produce 7-aminocephalosporanoic acid.

Fremgangsmåden ifølge opfindelsen belyses i det følgende ved udførelseseksempler: 8 143030The process according to the invention is illustrated in the following by way of example: 8

Eksempel 1Example 1

Fremstilling af natrium N-carbisobutoxycephalosporin C 05 ? S Ϊ /S\ H07C-C-(CH7U-C-N--f η Δ , Δ O 0 NH " • J-N Λ-CH7-0-C-CH7 c=o 0^ 10 ? C02Na I 6 ch3 ch3 15 2900 liter dyrkningssubstrat indeholdende cephalosporin C blande des med 108 kg filtreringshjælpemiddel og 300 ml siliconeantiskumstof og filtreredes dernæst ved en pH-værdi på 6,9 ved 10°C.Preparation of sodium N-carbisobutoxycephalosporin C 05? S Ϊ / S \ H07C-C- (CH7U-CN - f η Δ, Δ O 0 NH "• JN Λ-CH7-0-C-CH7 c = o 0 ^ 10? C02Na I 6 ch3 ch3 15 2900 liters culture substrate containing cephalosporin C was mixed with 108 kg of filter aid and 300 ml of silicone antifoam and then filtered at a pH of 6.9 at 10 ° C.

Til det filtrerede medium sattes tilstrækkelig oxalsyre til at opnå en pH-værdi på 3,1. Efter denne tilsætning indstilledes pH-værdien 20 til 2 med tilsætning af 30% svovlsyre. Der tilsattes 54 kg frisk filtreringshjælpemiddel, og blandingen filtreredes. Det således opnåede filtrat ekstraheredes med 1/2 volumen methylisobutylketon (MIBK) ved en pH-værdi på 2 og fraskiltes dernæst. MIBK-fasen kastedes bort.To the filtered medium was added sufficient oxalic acid to obtain a pH of 3.1. After this addition, the pH was adjusted to 20 to 2 with the addition of 30% sulfuric acid. 54 kg of fresh filtration aid was added and the mixture was filtered. The filtrate thus obtained was extracted with 1/2 volume of methyl isobutyl ketone (MIBK) at a pH of 2 and then separated. The MIBK phase was discarded.

25 En fjerdedel volumen acetone tilsattes det ekstraherede medium, og pH-værdien indstilledes til 7,85 med en opløsning af natriumhydroxid. 2 kg isobutylchlorformiat pr. 1000 liter filtreret medium tilsattes langsomt under omrøring (et molært forhold på 5,9 mol isobutylchlorformiat pr. mol cephalosporin C). pH-værdien holdtes konstant 30 ved 7,8-8,0 ved tilsætning af 15% natriumhydroxid, og temperaturen holdtes i intervallet 0-10°C under tilsætningen. Omrøring fortsattes, indtil pH-værdien blev konstant uden tilsætning af yderligere natriumhydroxid, i et tidsrum på ca. 2 timer.A quarter volume of acetone was added to the extracted medium and the pH was adjusted to 7.85 with a solution of sodium hydroxide. 2 kg of isobutyl chloroformate per 1000 liters of filtered medium was added slowly with stirring (a molar ratio of 5.9 moles of isobutyl chloroformate per mole of cephalosporin C). The pH was kept constant at 7.8-8.0 by the addition of 15% sodium hydroxide, and the temperature was kept in the range of 0-10 ° C during the addition. Stirring was continued until the pH became constant without the addition of additional sodium hydroxide, for a period of approx. 2 hours.

pH-værdien indstilledes til 2 ved tilsætning af 13% svovlsyre, 35 og det acylerede medium ekstraheredes med 1/2 volumen MIBK.The pH was adjusted to 2 by the addition of 13% sulfuric acid, 35 and the acylated medium was extracted with 1/2 volume of MIBK.

MIBK-fasen vaskedes med vand og koncentreredes dernæst til ca.The MIBK phase was washed with water and then concentrated to ca.

1/3 af det oprindelige volumen ved 36°C i vakuum. Vandindholdet af koncentratet var 0,2% (Karl Fishers metode).1/3 of the original volume at 36 ° C in vacuo. The water content of the concentrate was 0.2% (Karl Fisher's method).

143030 9143030 9

Koncentratet afkøledes, og en opløsning af natriumethylhexanoat i MIBK tilsattes til en pH-værdi pi 4,8. Natriumsaltet af en carbiso-butoxycephalosporin C udfældede og opsamledes ved filtrering. Bundfaldet vaskedes med MIBK, opslæmmedes i petroleumether, filtreredes 05 og tørredes i en vakuumovn ved 40°C til 60°C, hvorved der fremkom 7,2 kg produkt. Undersøgelse af det tilbageblevne medium viste tilstedeværelse af mindre end 1% cephalosporin C aktivitet. Produktet, som opsamledes, skønnedes at være 42% til 50% ren natrium n-carbiso-butoxycephalosporin C. Produktet var af tilstrækkelig renhed til den 10 efterfølgende fremstilling af 7-aminocephalosporansyre.The concentrate was cooled and a solution of sodium ethyl hexanoate in MIBK was added to a pH of 4.8. The sodium salt of a carbisobutoxycephalosporin C precipitated and collected by filtration. The precipitate was washed with MIBK, suspended in petroleum ether, filtered 05 and dried in a vacuum oven at 40 ° C to 60 ° C to yield 7.2 kg of product. Examination of the remaining medium showed the presence of less than 1% cephalosporin C activity. The product collected was estimated to be 42% to 50% pure sodium n-carbisobutoxycephalosporin C. The product was of sufficient purity for the subsequent 7-aminocephalosporanic acid preparation.

Eksempel 2Example 2

Fremstilling af natrium N-carbisobutoxycephalosporin CPreparation of sodium N-carbisobutoxycephalosporin C

Den i eksempel 1 beskrevne fremgangsmåde gentoges, idet der 15 i stedet for et molforhold pi 5,9:1 mellem isobutylchlorformiat og cephalosporin C anvendtes et molært forhold pi 4,5:1, og der fremkom 10,4 kg produkt. Undersøgelse af det tilbageblevne dyrkningsmedium efter ekstraktion viste tilstedeværelse af mindre end 14% cephalosporin C aktivitet.The procedure described in Example 1 was repeated, instead of a molar ratio of 5.9: 1 between isobutyl chloroformate and cephalosporin C, a molar ratio of 4.5: 1 was used and 10.4 kg of product was obtained. Examination of the residual culture medium after extraction showed the presence of less than 14% cephalosporin C activity.

2020

Eksempel 3Example 3

Fremstilling af N-CN'-butylcarbamoyQcephalosporin C 25 H OH /Sv » li » / \ ho9c-c-(Ch7u-c-n--r i 2 , v 2'3 0 NH " , i- —ch2-o-c-ch3Preparation of N-CN'-butylcarbamoylcephalosporin C 25 H OH / Sv »li» / \ ho9c-c- (Ch7u-c-n - r in 2, v 2'30 NH ", i- -ch2-o-c-ch3

C=0 SC = 0 S

30 . I30. IN

NH C07Na I u iCIV3 ch3 35 10 143030 2900 liter dyrkningssubstrat indeholdende cephalosporin C blandedes med 108 kg filtreringshjælpemiddel og 300 ml siliconeantiskumstof og filtreredes dernæst ved en pH-værdi på 6,9 ved 10°C.NH07Na I uCIV3 ch3 35 10 143030 2900 liters of culture medium containing cephalosporin C was mixed with 108 kg of filter aid and 300 ml of silicone antifoam and then filtered at a pH of 6.9 at 10 ° C.

Til det filtrerede medium sattes tilstrækkelig oxalsyre til at opnå 05 en pH-værdi pi 3,1. Efter denne tilsætning indstilledes pH-værdien til 2 ved tilsætning af 30% svovlsyre. Der tilsattes 54 kg frisk filtreringshjælpemiddel, og blandingen filtreredes. Det således opnåede filtrat ekstraheredes med 1/2 volumen methylisobutylketon (MIBK) ved en pH-værdi på 2 og fraskiltes dernæst. MIBK-fasen kstedes 10 bort.To the filtered medium, sufficient oxalic acid was added to obtain 05 a pH of 3.1. After this addition, the pH was adjusted to 2 by the addition of 30% sulfuric acid. 54 kg of fresh filtration aid was added and the mixture was filtered. The filtrate thus obtained was extracted with 1/2 volume of methyl isobutyl ketone (MIBK) at a pH of 2 and then separated. The MIBK phase was removed.

Et kvart volumen acetone sattes til det ekstraherede medium, og pH-værdien indstilledes til 7,85 med en opløsning af natriumhydroxid. n-Butylisocyanat (2 kg/1000 I medium) tilsattes langsomt under omrøring (et molært forhold på ca. 6,1 mol n-butylisocyanat 15 pr. mol cephalosporin C).A quarter volume of acetone was added to the extracted medium and the pH was adjusted to 7.85 with a solution of sodium hydroxide. n-Butyl isocyanate (2 kg / 1000 l medium) was added slowly with stirring (a molar ratio of about 6.1 moles of n-butyl isocyanate per mole of cephalosporin C).

pH-værdien holdtes konstant ved 7,8 til 8,0 ved tilsætning af 15% natriumhydroxid, og temperaturen holdtes i intervallet 0-10°C under tilsætning. Omrøring fortsattes, indtil pH-værdien forblev konstant uden yderligere tilsætning af natriumhydroxid, i et tidsrum på 20 ca. 2 timer.The pH was kept constant at 7.8 to 8.0 by the addition of 15% sodium hydroxide, and the temperature was maintained in the range 0-10 ° C during addition. Stirring was continued until the pH remained constant without further addition of sodium hydroxide, for a period of about 20 minutes. 2 hours.

pH-værdien indstilledes til 2 ved tilsætning af 30% svovlsyre, og det acylerede medium ekstraheredes med 3/4 volumen n-butanol. Butanolfasen vaskedes med vand og koncentreredes dernæst til ca. det halve af udgangsvoluminet i 36°C i vakuum. Koncentratets vand-25 indhold var negligeabelt.The pH was adjusted to 2 by the addition of 30% sulfuric acid and the acylated medium was extracted with 3/4 volume of n-butanol. The butanol phase was washed with water and then concentrated to ca. half of the output volume in 36 ° C in vacuo. The water content of the concentrate was negligible.

Koncentratet afkøledes, og en opløsning af natriumethylhexanoat i n-butanol tilsattes til en pH-værdi på 4,8. Natriumsaltet af N,N'--butylcarbamoylcephalosporin C udfældede og opsamledes ved filtrering. Bundfaldet vaskedes med butanol, opslæmmedes i petroleumether, 30 vaskedes med acetone, filtreredes og tørredes i en vakuumovn ved 40-60°C til frembringelse af produktet. Undersøgelse af det tilbageblevne medium viste tilstedeværelse af mindre end 15% cephalosporin C aktivitet. Produktet var tilstrækkelig rent til efterfølgende fremstilling af 7-ACA. Det optrådte som di-syren.The concentrate was cooled and a solution of sodium ethyl hexanoate in n-butanol was added to a pH of 4.8. The sodium salt of N, N '- butylcarbamoylcephalosporin C precipitated and collected by filtration. The precipitate was washed with butanol, suspended in petroleum ether, washed with acetone, filtered and dried in a vacuum oven at 40-60 ° C to give the product. Examination of the remaining medium showed the presence of less than 15% cephalosporin C activity. The product was sufficiently pure for subsequent preparation of 7-ACA. It appeared as the di-acid.

35 Analyse beregnet for C2.jHgQN4OgS.H2O: C 47,36; H 6,06; N 10,54; H^O 3,38.Analysis calculated for C₂jHHQN4O₂S.H₂O: C, 47.36; H, 6.06; N, 10.54; H 3 O 3.38.

C 47,85; H 6,52; N 10,54; ^O 3,48.C, 47.85; H, 6.52; N, 10.54; O 3.48.

Claims (4)

143030 Eksempel 4 Fremstilling af natrium N-CN'-phenylcarbamoyQ-cephalosporin C Fremgangsmåden ifølge eksempel 3 gentoges, idet der i stedet 05 for et molært forhold på 6,1:1 mellem n-butylisocyanat og cephalosporin C anvendtes et molært forhold på 7:1 mellem phenylisocyanat og cephalosporin C. Der fremkom et produkt, som var tilfredsstillende for spaltning til 7-ACA. Undersøgelse af det tilbageblevne medium efter ekstraktion viste tilstedeværelse af mindre end 15% cephalo-10 sporin C aktivitet. Det blev undersøgt som di-syren. Analyse beregnet for C23H26N4°9S: C 51,68; H 4,90; N 10,48; S 6,00. C 51,63; H 5,27; N 10,62; S 6,14.Example 4 Preparation of Sodium N-CN'-phenylcarbamoyQ-cephalosporin C The procedure of Example 3 was repeated, using instead of a molar ratio of 6.1: 1 between n-butyl isocyanate and cephalosporin C, a molar ratio of 7: 1 between phenyl isocyanate and cephalosporin C. A product was found which was satisfactory for cleavage to 7-ACA. Examination of the remaining medium after extraction showed the presence of less than 15% cephalo-10 sporin C activity. It was investigated as the diacid. Analysis calculated for C 23 H 26 N 4 O 9 S: C 51.68; H, 4.90; N, 10.48; S, 6.00. C, 51.63; H, 5.27; N, 10.62; S 6.14. 15 Patentkrav15 Patent claims 1. Fremgangsmåde til in situ fremstilling af et cephalosporin C-derivat med den almene formel 20 H OH ~ , ... ^S \ H0oC-C- (CH0) ,-C-N--r 1 l 1 £ s o NH " 111 . V. A-CH--0-C-CH, C=0 -N 2 6A process for in situ preparation of a cephalosporin C derivative of the general formula 20 H OH ~, ... ^ S \ H0OC-C- (CHO), -CN - r 1 l 1 £ SO NH "111. V. A-CH - 0-C-CH, C = 0 -N 2 6 25 B ° I co2h hvor B betegner en gruppe med formlen -NHR eller -OR, idet R be-30 tegner al kyl med 1-10 carbonatomer eller en gruppe med formlen -oc:B is in CO 2 h where B represents a group of formula -NHR or -OR, where R represents all alkyl of 1-10 carbon atoms or a group of formula -oc:
DK352569A 1968-07-01 1969-06-30 PROCEDURE FOR IN-SITU PREPARATION OF A CEPHALOSPORIN C DERIVATE DK143030C (en)

Priority Applications (2)

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DK123471A DK143031C (en) 1968-07-01 1971-03-16 METHOD OF PREPARING 7-AMINOCEPHALOSPORANIC ACID
DK423478A DK423478A (en) 1968-07-01 1978-09-25 CEPHALOSPORIN C-DERIVATIVES

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BE793037A (en) * 1971-12-23 1973-06-20 Fujisawa Pharmaceutical Co PROCESS FOR THE PREPARATION OF 7-ACYLAMINO-3-SUBSTITUE-3-CEPHEM-4-CARBOXYLIC ACID DERIVATIVES AND NEW PRODUCTS THUS OBTAINED
GB1425081A (en) * 1972-06-27 1976-02-18 Fujisawa Pharmaceutical Co Antibiotics ws-3442a, b,c,d and e and n-acyl derivatives thereof
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