HRP940690A2 - Process for the preparation of cefodizime - Google Patents

Process for the preparation of cefodizime Download PDF

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HRP940690A2
HRP940690A2 HRP-2061/86A HRP940690A HRP940690A2 HR P940690 A2 HRP940690 A2 HR P940690A2 HR P940690 A HRP940690 A HR P940690A HR P940690 A2 HRP940690 A2 HR P940690A2
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Croatia
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formula
process according
compound
solvent
base
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HRP-2061/86A
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Ottimar Jaenicke
Hans Wagner
Manfred Worm
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Hoechst Ag
Ruhrchemie Ag
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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Cefodizim (HR 221) formule Cefodisim (HR 221) formula

[image] [image]

(cefodizim) (cefodisim)

je antibiotik, kojeg je priprava i dobra antibiotska aktivnost je poznata iz literature. Možemo ga dobiti kemijskom pretvorbom na karboksilnoj skupini aktivirane ATS formule is an antibiotic whose preparation and good antibiotic activity are known from the literature. It can be obtained by chemical conversion on the carboxyl group of the activated ATS formula

[image] [image]

(ATS) (ATS)

ATS= 2-(2-amino-tiazol-4-il)-2-(metoksiimino)-octena kiselina s TACS formule ATS= 2-(2-amino-thiazol-4-yl)-2-(methoxyimino)-acetic acid with TACS formula

[image] [image]

(TACS) (TAX)

TACS= 7-amino-3-(4-metil-5-karboksimetil-1,3-tiazol-2-il-tiometil)-cef-3-em-4-karboksilna kiselina. Posebno prikladan postupak za pripravu cefalosporina opisan je u EP-A 23 453. Ako se njega uporabi za pripravu cefodizima , pored željenog cefodizima nastaje sporedni proizvod reda veličine oko 5 do 15 %. Sadržaj sporednog proizvoda možemo smanjiti različitim uzastopnim stupnjevima čišćenja, ali se ipak ne može potpuno ukloniti iz cefodizima. Osim toga ovi su postupci čišćenja (npr. kromatografija, prekristalizacija ) skupi, jer su dugotrajni i znatno smanjuju ukupni dobitak. TACS= 7-amino-3-(4-methyl-5-carboxymethyl-1,3-thiazol-2-yl-thiomethyl)-cef-3-em-4-carboxylic acid. A particularly suitable procedure for the preparation of cephalosporins is described in EP-A 23 453. If it is used for the preparation of cefodisim, in addition to the desired cefodisim, a side product of the order of 5 to 15% is formed. The content of the side product can be reduced by different successive stages of purification, but still it cannot be completely removed from cefodis. In addition, these cleaning procedures (e.g. chromatography, recrystallization) are expensive, because they are long-lasting and significantly reduce the total gain.

Zato su nadalje izveli mnogo, kako bi promijenili reakcijske parametre, s ciljem, da bi se spriječila tvorba sporednog proizvoda, kao npr. variranjem omjera molova, temperature, vremena reakcije , otapala , baze koju je potrebno u danom primjeru dodati, aktiviranog sredstva ili s drugim dodacima . Niti jedan od ovih pokusa nije bio uspješan. Tvorba spomenutog sporednog proizvoda nije se mogla smanjiti . That's why they carried out a lot, in order to change the reaction parameters, with the aim of preventing the formation of a side product, such as by varying the ratio of moles, temperature, reaction time, solvent, the base that needs to be added in the given example, the activated agent or with other additions. None of these attempts were successful. The formation of the mentioned secondary product could not be reduced.

Kod ispitivanja daljnjih dodataka smo iznenada ustanovili, da se dodatkom sililirnog sredstva TACS-u skoro potpuno sprječava tvorba sporednog proizvoda. When testing further additives, we suddenly found that the addition of a silylating agent to TACS almost completely prevents the formation of a side product.

Izum se, dakle, odnosi na postupak za pripravu cefodizima formule The invention therefore relates to a process for the preparation of cefodisim formula

[image] [image]

(cefodizim) (cefodisim)

naznačen time, da indicated by that

(a) najprije u organskom otapalu i u danom primjeru u prisutnosti baze spoj formule II (ATS) (a) first in an organic solvent and in the given example in the presence of a base compound of formula II (ATS)

[image] [image]

u kojem R-1 predstavlja vodik ili amino zaštitnu skupinu i A vodikov atom ili ekvivalent alkalijskog ili zemnoalkalijskog metala, amonijaka ili organske dušikove baze, kemijski pretvorimo sa spojem formule III in which R-1 represents hydrogen or an amino protecting group and A is a hydrogen atom or an equivalent of an alkali or alkaline earth metal, ammonia or an organic nitrogen base, chemically converted with the compound of formula III

R-SO2-Hal R-SO2-Hal

u kojoj umjesto R stoji u danom primjeru supstituiran alkilni, arilni ili aralkilni ostatak i Hal predstavlja atom halogena, in which instead of R stands in the given example a substituted alkyl, aryl or aralkyl residue and Hal represents a halogen atom,

(b) u organskom otapalu i u danom primjeru u prisutnosti baze sa spojem formule I (TACS) (b) in an organic solvent and in the given example in the presence of a base with a compound of formula I (TACS)

[image] [image]

u kojoj ima A gornje značenje , kemijski pretvorimo sa sililirnim sredstvom i in which A has the above meaning, chemically convert with a silyl agent i

(c) oba prema (a) i (b) nastala proizvoda kemijski pretvorimo u njihovim reakcijskim otopinama i u konačnom proizvodu formule I odcijepimo u danom primjeru prisutnu zaštitnu skupinu R1. (c) we chemically convert both of the products obtained according to (a) and (b) in their reaction solutions and in the final product of formula I we cleave off the protective group R1 present in the given example.

A pored vodika i amonijaka može se nalaziti također ekvivalent alkalijskog metala, kao npr. natrija ili kalija, zemnoalkalijskog metala, kao npr. kalcija i magnezija, ili organske dušikove baze, kao npr. dietil-, trimetil-, trietil-,metil-, propil-, N,N-dimetiletanol- ili etanolamina. And besides hydrogen and ammonia, there can also be an equivalent of an alkali metal, such as sodium or potassium, an alkaline earth metal, such as calcium and magnesium, or an organic nitrogen base, such as diethyl-, trimethyl-, triethyl-, methyl-, propyl-, N,N-dimethylethanol- or ethanolamine.

Kao zaštitne skupine R1 u obzir dolaze takve, koje su u cefalosporinskoj ili peptidnoj kemiji opisane kao amino zaštitne skupine, npr. one, koje su spomenute u EP-A-23 453, str. 3, redovi 43 do 63. Ponajprije uporabimo u smislu izuma spojeve, u kojima umjesto R1 stoji vodik. Neobaveznom zaštitom amino skupine možemo uštedjeti dva reakcijska stupnja ( zaštita, odcjepljenje), što dovodi do još šireg povećanja dobitka . Suitable protecting groups R1 are those described in cephalosporin or peptide chemistry as amino protecting groups, for example those mentioned in EP-A-23 453, p. 3, lines 43 to 63. First of all, let's use in the sense of the invention the compounds, in which instead of R1 is hydrogen. By optional protection of the amino group, we can save two reaction steps (protection, separation), which leads to an even wider increase in profit.

Kao spojevi formule III u obzir dolaze svi koji su u literaturi opisani kao prikladni za kemijsku pretvorbu s karboksilnom, kao npr. metansulfonilklorid ili tozilklorid, pri čemu vjerojatno nastaje aktiviran ostatak karboksilne kiseline -COOSO2-R. Spojevi koji imaju prednost zbog dobre reakcijske sposobnosti i lake dostupnosti su spojevi kao p-tozilklorid i također fenilsulfonilklorid. Nadalje spojevi koji imaju prednost su formule III , u kojima umjesto Hal stoji klor. As compounds of formula III, all those described in the literature as suitable for chemical conversion with carboxylic acid, such as methanesulfonyl chloride or tosyl chloride, are considered, whereby an activated carboxylic acid residue -COOSO2-R is probably formed. Compounds that are preferred due to good reactivity and easy availability are compounds such as p-tosyl chloride and also phenylsulfonyl chloride. Furthermore, the preferred compounds are formula III, in which chlorine is used instead of Hal.

Kemijsku pretvorbu između spoja formule II i spoja formule III možemo izvesti u bezvodnom organskom otapalu, kao npr. acetonu, etilacetatu, tetrahidrofuranu, acetonitrilu, tatraklorugljiku, metilenkloridu, toluolu, dioksanu, izopropileteru, N-metilpirolidonu, dimetilformadidu, ponajprije u dimetilacetamidu pri temperaturama između oko - 30 do 0ºC, ponajprije između -10 i 15ºC. The chemical conversion between the compound of formula II and the compound of formula III can be carried out in an anhydrous organic solvent, such as acetone, ethyl acetate, tetrahydrofuran, acetonitrile, carbon tetrachloride, methylene chloride, toluene, dioxane, isopropyl ether, N-methylpyrrolidone, dimethylformamide, preferably in dimethylacetamide at temperatures between around -30 to 0ºC, preferably between -10 and 15ºC.

Ako uporabimo spoj formule II u obliku slobodne kiseline ( A = vodik ), smišljeno je,da dodamo bazu, ponajprije organsku dušikovu bazu, kao npr. trietilamin, N,N-dimetilanilin, tributilamin, N-metil-morfolin, piridin, pikolin ili također npr. natrijev ili kalijev karbonat ili bikarbonat naročito trietilamin. Bazu ne treba dodavati, ako uporabimo karboksilnu kiselinu formule II u obliku jedne od gore navedenih soli. If we use the compound of formula II in the form of a free acid (A = hydrogen), it is thought to add a base, primarily an organic nitrogen base, such as triethylamine, N,N-dimethylaniline, tributylamine, N-methyl-morpholine, pyridine, picoline or also, for example, sodium or potassium carbonate or bicarbonate, especially triethylamine. The base does not need to be added, if we use the carboxylic acid of formula II in the form of one of the above-mentioned salts.

Daljnju kemijsku pretvorbu sada izvedemo tako , da spoj formule I (TACS) u bezvodnom organskom otapalu, kao npr. metilenkloridu, dimetilacetamidu, metil-terc-burileteru, metilizobutilketonu, butilacetatu ili amilacetetu, naročito metilenkloridu ili metil-terc-butileteru, kemijski pretvorimo s oko 3 molarna ekvivalenta sililirnog sredstva, ponajprije s trimetilklorsilanom, u prisutnosti - obzirom na sililirno sredstvo - približno stehiometrijske količine organske dušikove baze, naročito trietilamina, i nato pretvorimo s karboksilnom kiselinom formule II, aktiviranu kemijskom pretvorbom sa spojem formule III. Further chemical conversion is now performed by chemically converting the compound of formula I (TACS) in an anhydrous organic solvent, such as methylene chloride, dimethylacetamide, methyl tert-butyl ether, methyl isobutyl ketone, butyl acetate or amyl acetate, especially methylene chloride or methyl tert-butyl ether, with about 3 molar equivalents of a silylating agent, preferably with trimethylchlorosilane, in the presence - considering the silylating agent - of an approximately stoichiometric amount of an organic nitrogen base, especially triethylamine, and then converted with a carboxylic acid of formula II, activated by chemical conversion with a compound of formula III.

Umjesto trimetilklorsilana možemo uporabiti druga i sililirna sredstva , kao npr., bis-trimetilsilil-acetamid, diklordimetilsilan , triklormetilsilan ili N,N-bistrimetilsililureu, pri čemu od ovih daljnjih sililirnih sredstava prednost ima bis-trimetilsililacetamid. Mali suvišak sililirnog sredstva, koji prelazi 3 molarna ekvivalenta, ne šteti pretvorbi. Instead of trimethylchlorosilane, we can use other silylating agents, such as, for example, bis-trimethylsilyl-acetamide, dichlorodimethylsilane, trichloromethylsilane or N,N-bistrimethylsilylurea, and of these further silylating agents, bis-trimethylsilylacetamide is preferable. A small excess of silylating agent, exceeding 3 molar equivalents, does not harm the conversion.

Kod uporabe bis-trimetilsililacetamida ili N, N - bis-trimetilsililuree kod sililiranja nije potrebno dodavati bazu, jer se u tom slučaju ne pojavi kloridna kiselina, koju je potrebno vezati. When using bis-trimethylsilylacetamide or N, N - bis-trimethylsilylurea during silylation, it is not necessary to add a base, because in that case no hydrochloric acid appears, which needs to be bound.

Sililiranje spoja formule I izvodimo pri temperaturama između oko 20 do 25º C . Možemo je pustiti također da naraste npr. i na oko 40º C (vrelište metilenklorida ). The silylation of the compound of formula I is carried out at temperatures between about 20 to 25º C. We can also let it grow, for example, to around 40º C (boiling point of methylene chloride).

Aktivirani ATS zajedno sa sililiranim TACS , spremimo smišljeno tako, da pri temperaturama između oko -20 do 0º C, ponajprije između -10 do -12º C, otopini aktiviranog ATS i polako dodajemo otopini sililirnog TACS , da se toplina nastala reakcijom može dobro odvoditi, npr. u vremenskom intervalu 1/4 do 2 sata. Poslije kratkog naknadnog miješanja reakcijsku smjesu na poznati način obradimo. Tako je možemo npr. uliti u vodu, kojoj pH održavamo pri oko 6,0 do 7,5 s dodatkom npr. organske dušikove baze, pogotovo trietilamina. Poslije odvajanja faza, organsku fazu onda možemo još jednom ekstrahirati s vodom u kojoj je otopljen natrijev acetat. Iz sjedinjenih organskih faza, koje možemo u damom primjeru još razbistriti, npr. s aktivnim ugljenom, pH podesimo na vrijednost od oko 2,8 s dodatkom mineralne kiseline, npr. sulfatne kiseline, i onda možemo cefodizim istaložiti kao slobodnu kiselinu. Activated ATS together with silylated TACS should be prepared so that at temperatures between -20 to 0º C, preferably between -10 to -12º C, to the solution of activated ATS and slowly added to the solution of silylated TACS, so that the heat generated by the reaction can be well dissipated. eg in a time interval of 1/4 to 2 hours. After a short subsequent mixing, the reaction mixture is processed in a known manner. So we can, for example, pour it into water, the pH of which we maintain at around 6.0 to 7.5 with the addition of, for example, an organic nitrogen base, especially triethylamine. After separating the phases, the organic phase can then be extracted once more with water in which sodium acetate is dissolved. From the combined organic phases, which we can further clarify in this example, e.g. with activated carbon, adjust the pH to a value of about 2.8 with the addition of a mineral acid, e.g. sulfuric acid, and then we can precipitate cefodisim as a free acid.

Ako uporabimo karboksilnu kiselinu formule II s amino zaštitnom R1, prije obrade potrebno je ovaj ostatak još na način poznat iz literature. If we use a carboxylic acid of formula II with an amino protecting R1, this residue is required before processing in a manner known from the literature.

Poslije sušenja pri malo povišenoj temperaturi i u vakuumu dobivamo kiselinu cefodizima u vrlo čistom obliku. After drying at a slightly elevated temperature and in a vacuum, we get cefodis acid in a very pure form.

Pored već gore spomenutog neočekivanog smanjenja sporednih proizvoda na sadržaj, koji je daleko ispod 1 %, spomenimo još i to, da npr. u izvedbenim primjerima 8 do 12 već spomenutog EP-A-23 453, pri aceliranju upotrebljavaju reakcijske temperature između -70 do -72ºC. In addition to the above-mentioned unexpected reduction of side products to a content far below 1%, let us also mention that, for example, in embodiments 8 to 12 of the already mentioned EP-A-23 453, reaction temperatures between -70 to -70 -72ºC.

Suprotno tome, moguće je, da kemijsku pretvorbu u smislu izuma izvedemo pri temperaturama od oko -20 do 0ºC, a da kod toga ne bi došlo do pogoršanja kvalitete ili dobitka. Ova činjenica za tehničku je proizvodnju cefodizima vrlo značajna, jer su s time povezani kraće vrijeme zadržavanja i manji kapacitet hlađenja. On the contrary, it is possible to carry out the chemical conversion in terms of the invention at temperatures from about -20 to 0ºC, without any deterioration in quality or profit. This fact is very significant for the technical production of cefodis, because it is associated with a shorter retention time and lower cooling capacity.

Primjer 1 Example 1

Stupanj 1 Degree 1

17,5 kg (87,1 mola) ATS u 52 kg dimetilacetamida prevedemo s 8,95 kg ( 88,6 mola ) trietilamina u amonijevu sol pri temperaturi 20 do 22º C i vremenom miješanja 30 minuta. 17.5 kg (87.1 moles) of ATS in 52 kg of dimethylacetamide are converted with 8.95 kg (88.6 moles) of triethylamine into the ammonium salt at a temperature of 20 to 22º C and a mixing time of 30 minutes.

12,9 kg (68,0 mola) p-toluolsulfoklorida u tijeku 30 minuta pri 20 do 25ºC otopimo u 13,2 kg dimetilacetamida, ovu otopinu pustimo dotjecati u suspenziju trietilamonijeve soli ATS 30 minuta pri -10 do -14ºC i onda još 2,5 sata miješamo. Dissolve 12.9 kg (68.0 moles) of p-toluenesulfochloride in 13.2 kg of dimethylacetamide over the course of 30 minutes at 20 to 25ºC, let this solution flow into the triethylammonium salt suspension ATS for 30 minutes at -10 to -14ºC and then for another 2 , we mix for 5 hours.

Stupanj 2 Degree 2

23,7 kg (59,0 mola ) TACS suspendiramo u 212 kg metilenklorida, pustimo dotjecati 19,7 kg (181,0 mola) trimetilklorsilana pri temperaturi 20 do 25ºC, i 30 minuta pri temperaturi 20 do 41ºC (temperatura refluksa metilenklorida) dodajemo 18,2 kg (180,0 mola ) trietilamina. We suspend 23.7 kg (59.0 moles) of TACS in 212 kg of methylene chloride, let 19.7 kg (181.0 moles) of trimethylchlorosilane flow in at a temperature of 20 to 25ºC, and for 30 minutes at a temperature of 20 to 41ºC (reflux temperature of methylene chloride) add 18.2 kg (180.0 moles) of triethylamine.

Nakon dodavanja otopinu brzo ohladimo na -15ºC i otopinu aktivirane ATS, dobivenu u prvom stupnju, dodajemo 30 minuta pri -10 do -12ºC. Poslije vremena od 5 minutnog miješanja pustimo dotjecati reakcijsku smjesu u smjesu 143 l vode i 19,3 kg trietilamina, pri čemu održavamo pH vrijednost između 6 i 7,5. Poslije odvajanja faza, metilenkloridnu fazu još jednom ekstrahiramo s 70 l vode, u kojoj je otopljeno 2,2 kg natrijeva acetata · 3 H2O, i iz sjedinjenih vodenih faza poslije razbistravanja s 1,2 kg aktivnog ugljena i 1,2 kg dikalita i s dodatkom 18 %-ne sulfatne kiseline dok ne postignemo pH vrijednost od 2,8, istaložimo cefodizim u obliku slobodne kiseline. Nakon filtriranja i sušenja pri 40ºC i 133 mbara dobijemo 30,6 kg cefodizima čistoće 96 do 97 površinskih % prema HPLC-analizi . After the addition, the solution is quickly cooled to -15ºC and the activated ATS solution, obtained in the first step, is added for 30 minutes at -10 to -12ºC. After 5 minutes of mixing, let the reaction mixture flow into the mixture of 143 l of water and 19.3 kg of triethylamine, while maintaining the pH value between 6 and 7.5. After separating the phases, the methylene chloride phase is extracted once again with 70 l of water, in which 2.2 kg of sodium acetate · 3 H2O is dissolved, and from the combined aqueous phases after clarification with 1.2 kg of activated carbon and 1.2 kg of dicalcium and with the addition of 18% sulfuric acid until we reach a pH value of 2.8, we precipitate cefodisim in the form of free acid. After filtering and drying at 40ºC and 133 mbar, we obtain 30.6 kg of cefodisim with a purity of 96 to 97 surface % according to HPLC analysis.

Primjer 2 Example 2

Stupanj 1 (odgovara podacima u primjeru 1.) Level 1 (corresponds to the data in example 1.)

Stupanj 2 Degree 2

23,7 kg (59,0 mola) TACS suspendiramo u 212 kg metilenklorida i dodajemo 36,0 kg (177,0 mola) bistrimetilsililacetamida. Miješamo 30 minuta pri 20 do 25ºC, bistru otopimo ohladimo na -15ºC i tijekom 30 minuta pri -10 do -20ºC dodajemo otopinu ne aktivirane ATS, dobivene prema stupnju 1. Nakon 5 minutnog miješanja pustimo dotjecati reakcijsku smjesu, 5 do 10 minuta, u 143 l vode i istovremeno održavamo pH vrijednost s trietilaminom između 6,0 i 7,7. Nakon odvajanja faza, organsku fazu još jednom ekstrahiramo s 70 kg vode koja sadrži 2,2 kg natrijeva acetata 3 H20. Sjedinjene vodene faza razbistrimo s 1,2 kg aktivnog ugljena i 1,2 kg dikalita, te dodatkom 18 %-ne sulfatne kiseline dok nije postignuta pH vrijednost od 2,8, istaložimo proizvod. Nakon filtriranja i sušenja pri 40ºC i 133 mbara dobijemo 30,0 kg cefodizima u obliku slobodne kiseline čistoće 95 do 97 površinskih % prema HPLC-analizi. 23.7 kg (59.0 moles) of TACS are suspended in 212 kg of methylene chloride and 36.0 kg (177.0 moles) of bistrimethylsilylacetamide are added. Stir for 30 minutes at 20 to 25ºC, cool the clear solution to -15ºC and during 30 minutes at -10 to -20ºC add the solution of unactivated ATS, obtained according to step 1. After 5 minutes of mixing, let the reaction mixture flow for 5 to 10 minutes in 143 l of water and at the same time we maintain the pH value with triethylamine between 6.0 and 7.7. After separating the phases, the organic phase is extracted once again with 70 kg of water containing 2.2 kg of sodium acetate 3 H20. Clarify the combined aqueous phases with 1.2 kg of activated carbon and 1.2 kg of dicalcium, and by adding 18% sulfuric acid until a pH value of 2.8 is reached, precipitate the product. After filtering and drying at 40ºC and 133 mbar, we obtain 30.0 kg of cefodisim in the form of free acid with a purity of 95 to 97 surface % according to HPLC analysis.

Claims (14)

1. Postupak za pripravu cefodizima formule [image] (cefodizim) naznačen time , da (a) najprije u organskom otapalu i u danom primjeru u prisutnosti baze, spoj formule II (ATS) [image] u kojem R1 predstavlja vodik ili amino zaštitnu skupinu i A vodikov atom ili ekvivalent alkalijskog ili zemnoalkalijskog metala, amonijaka ili organske dušikove baze, kemijski pretvorimo sa spojem formule III R-SO2-Hal u kojoj umjesto R stoji u danom primjerku supstituiran alkilni, arilni ostatak i HaL predstavlja atom halogena , (b) u organskom otapalu i u danom primjeru u prisutnosti baze sa spojem formule I (TACS) [image] u kojoj ima A gornje značenje , kemijski pretvorimo sa sililirnim sredstvom i (c) oba prema (a) i (b) nastala proizvoda kemijski pretvorimo u njihovim reakcijskim otopinama i u konačnom proizvodu formule I odcijepimo u danom primjeru prisutnu zaštitnu skupinu R1.1. Procedure for preparation of cefodisim formula [image] (cefodisim) indicated by that, yes (a) first in an organic solvent and in the given example in the presence of a base, the compound of formula II (ATS) [image] in which R1 represents hydrogen or an amino protecting group and A is a hydrogen atom or an equivalent of an alkali or alkaline earth metal, ammonia or an organic nitrogen base, chemically converted with the compound of formula III R-SO2-Hal in which instead of R stands in the given example a substituted alkyl, aryl residue and HaL represents a halogen atom, (b) in an organic solvent and in the given example in the presence of a base with a compound of formula I (TACS) [image] in which A has the above meaning, chemically convert with a silyl agent i (c) we chemically convert both of the products obtained according to (a) and (b) in their reaction solutions and in the final product of formula I we cleave off the protective group R1 present in the given example. 2. Postupak prema zahtjevu 1, naznačen time, da u spoju formule III umjesto R stoji p-tolil ili fenil i Hal je klor. 2. The process according to claim 1, characterized in that in the compound of formula III, p-tolyl or phenyl is used instead of R and Hal is chlorine. 3. Postupak prema zahtjevu 2 , naznačen time, da umjesto R stoji p-tolil. 3. Process according to claim 2, characterized in that instead of R stands p-tolyl. 4. Postupak prema zahtjevima 1 do 3, naznačen time, da je u spoju formule II (ATS) umjesto R1 i A stoje vodici. 4. Process according to claims 1 to 3, characterized in that in the compound of formula II (ATS) instead of R1 and A there are hydrogens. 5. Postupak prema zahtjevima 1 do 5, naznačen time, da je u stupnju postupka (a) uporabljeno otapalo aceton, dimetilacetamid, etilacetat, tetrahidrofuran, acetonitril, tetraklorugljik, metilenklorid, toluol, dioksan, izopropileter, N-metilpirolidon, dimetilformadid.5. The method according to claims 1 to 5, characterized in that the solvent acetone, dimethylacetamide, ethylacetate, tetrahydrofuran, acetonitrile, carbon tetrachloride, methylene chloride, toluene, dioxane, isopropyl ether, N-methylpyrrolidone, dimethylformamide is used in step (a). 6. Postupak prema zahtjevu 5, naznačen time, da je otapalo dimetilacetamid.6. The method according to claim 5, characterized in that the solvent is dimethylacetamide. 7. Postupak prema zahtjevima 1 do 6, naznačen time, da je sililirno trimetilklorsilan, diklordimetilsilan, triklormetilsilan, bis-trimetilsililacetamid ili N,N-bis-trimetilsililurea.7. Process according to claims 1 to 6, characterized in that silyl is trimethylchlorosilane, dichlorodimethylsilane, trichloromethylsilane, bis-trimethylsilylacetamide or N,N-bis-trimethylsilylurea. 8. Postupak prema zahtjevu 7, naznačen time, da je sililirno sredstvo trimetilklorsilan.8. The method according to claim 7, characterized in that the silylating agent is trimethylchlorosilane. 9. Postupak prema zahtjevima 7 do 8, naznačen time, da uporabimo 3 molarna ekvivalenta sililirnog sredstva u odnosu na TACS.9. The method according to claims 7 to 8, characterized in that we use 3 molar equivalents of the silylating agent in relation to TACS. 10. Postupak prema zahtjevima 1 do 8, naznačen time, da je u stupnju postupka (b) uporabljeno otapalo metilenklorid, dimetilacetamid, metil-terc-butileter , metilizobutilketon, butilacetat ili amilacetat.10. The process according to claims 1 to 8, characterized by the fact that methylene chloride, dimethylacetamide, methyl tert-butyl ether, methyl isobutyl ketone, butyl acetate or amyl acetate is used as a solvent in step (b). 11. Postupak prema zahtjevu 9, naznačen time, da je otapalo metilenklorid ili metil-terc-butileter.11. The method according to claim 9, characterized in that the solvent is methylene chloride or methyl tert-butyl ether. 12. Postupak prema zahtjevima 1 do 10, naznačen time, da je baza, koju dodajemo među pojedinačnim stupnjevima postupka, trietilamin. 12. The process according to claims 1 to 10, characterized in that the base, which is added between the individual stages of the process, is triethylamine. 13. Postupak prema zahtjevima 1 do 11, naznačen time, da izvedemo kemijsku pretvorbu stupnja postupka (a) pri temperaturama između oko -30 do 0ºC.13. The process according to claims 1 to 11, characterized in that we carry out the chemical conversion of process step (a) at temperatures between about -30 to 0ºC. 14. Postupak prema zahtjevima 1 do 12, naznačen time, da izvedemo kemijsku pretvorbu stupnja postupka (b) pri temperaturama između oko -20 do 0ºC.14. The process according to claims 1 to 12, characterized in that we carry out the chemical conversion of process step (b) at temperatures between about -20 to 0ºC.
HRP-2061/86A 1985-12-03 1994-10-19 Process for the preparation of cefodizime HRP940690B1 (en)

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Application Number Priority Date Filing Date Title
DE19853542644 DE3542644A1 (en) 1985-12-03 1985-12-03 METHOD FOR PRODUCING CEFODIZIM
YU206186A YU45807B (en) 1985-12-03 1986-12-02 PROCEDURE FOR PREPARATION OF CEFODISIM

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HRP940690A2 true HRP940690A2 (en) 1997-04-30
HRP940690B1 HRP940690B1 (en) 1998-10-31

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