LT3697B - Process for the manufacture of budesonide - Google Patents

Process for the manufacture of budesonide Download PDF

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Publication number
LT3697B
LT3697B LTIP1729A LTIP1729A LT3697B LT 3697 B LT3697 B LT 3697B LT IP1729 A LTIP1729 A LT IP1729A LT IP1729 A LTIP1729 A LT IP1729A LT 3697 B LT3697 B LT 3697B
Authority
LT
Lithuania
Prior art keywords
reaction
budesonide
methanol
catalyst
water
Prior art date
Application number
LTIP1729A
Other languages
English (en)
Inventor
Robert Gerrit Hofstraat
Petrus Hendricus Raijmakers
Pieter Vrijhof
Original Assignee
Astra Ab
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 Astra Ab filed Critical Astra Ab
Publication of LTIP1729A publication Critical patent/LTIP1729A/xx
Publication of LT3697B publication Critical patent/LT3697B/lt

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07JSTEROIDS
    • C07J71/00Steroids in which the cyclopenta(a)hydrophenanthrene skeleton is condensed with a heterocyclic ring
    • C07J71/0005Oxygen-containing hetero ring
    • C07J71/0026Oxygen-containing hetero ring cyclic ketals
    • C07J71/0031Oxygen-containing hetero ring cyclic ketals at positions 16, 17
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07JSTEROIDS
    • C07J5/00Normal steroids containing carbon, hydrogen, halogen or oxygen, substituted in position 17 beta by a chain of two carbon atoms, e.g. pregnane and substituted in position 21 by only one singly bound oxygen atom, i.e. only one oxygen bound to position 21 by a single bond
    • C07J5/0046Normal steroids containing carbon, hydrogen, halogen or oxygen, substituted in position 17 beta by a chain of two carbon atoms, e.g. pregnane and substituted in position 21 by only one singly bound oxygen atom, i.e. only one oxygen bound to position 21 by a single bond substituted in position 17 alfa
    • C07J5/0061Normal steroids containing carbon, hydrogen, halogen or oxygen, substituted in position 17 beta by a chain of two carbon atoms, e.g. pregnane and substituted in position 21 by only one singly bound oxygen atom, i.e. only one oxygen bound to position 21 by a single bond substituted in position 17 alfa substituted in position 16
    • C07J5/0092Normal steroids containing carbon, hydrogen, halogen or oxygen, substituted in position 17 beta by a chain of two carbon atoms, e.g. pregnane and substituted in position 21 by only one singly bound oxygen atom, i.e. only one oxygen bound to position 21 by a single bond substituted in position 17 alfa substituted in position 16 by an OH group free esterified or etherified

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Steroid Compounds (AREA)
  • Paper (AREA)
  • Load-Bearing And Curtain Walls (AREA)

Description

butanaliu dioksane, katalizatoriumi naudojant chloro perrūgštį. Produktas išskiriamas, reakcijos mišinį skiedžiant metileno chloridu. Neutralizavimas atliekamas, plaunant vandeniniu kalio karbonatu ir vandeniliu. Toliau seka tirpiklio nugarinimas ir kristalinimas iš eterio/ligroino. Tolimesnis produkto valymas atliekamas chromatografijos būdu, pvz. naudojant Sephadex tipo įrenginį. Pagrindiniais dioksano trūkumais yra jo skvarbumas pro odą, sugebėjimas sudaryti peroksidą. Kitu šio žinomo būdo trūkumu yra chloro perrūgštis, esanti stipriu oksidatoriumi. Naudojant šį katalizatorių, pablogėja reakcijos metu išsiskiriančio produkto kokybė. Dėl to, savo ruožtu, tolimesnis apdirbimas bei išgryninimas tampa sudėtingu ir brangiu.
Šio išradimo tikslas - sukurti naują būdą su žymiai kokybiškesne reakcija ir su paprastesnių bei ekonomiškesniu produkto išvalymo ir apdirbimo procesu.
Šį tikslą pasiekti leidžia šį išradimą atitinkantis procesas. Jo metu reakcija vykdoma acetonitrile, katalizatoriumi naudojant p-tolueno sulforūgštį.
Mažiau bazinio (palyginus su dioksanu) tirpiklio acetonitrilo ir silpnesnės, t.y. nesančios oksidatoriumi, p-tolueno sulforūgšties suderinimo dėka reakcija tampa žymiai kokybiškesnė. Palyginus su aukščiau aptartu dioksano bei chloro perrūgšties panaudojimu pagrįstu procesu, dabar išvalymas bei apdirbimas supaprastėja ir tampa ekonomiškesniais.
Pagal vieną iš patogiausių šio išradimo įgyvendinimo variantų reakcija nutraukiama, tuo tikslu papildomai įpilant vandens ir pakoreguojant reakcijos mišinio pH. Tai gali būti atliekama, į vandenį papildomai įpilant natrio hidrokarbonato. Tuomet įvyksta produkto kristalizacija. Kristalai nufiltruojami, ištirpinami metileno chloride ir metanolyje, o po to kristalizuojami, tuo tikslu įpilant tinkamo angliavandenilio, tokio, kai ligroinas, heksanas, cikloheksanas arba heptanas ir gaunamas nevalytas produktas. Atlikus jo perkristalinimą metanolyje/vandenyje, gaunamas grynas budezonidas.
Šį išradimą atitinkantis budezonido gamybos procesas vyksta dviem etapais.
Etapas. Nevalytas budezonidas.
Įvykdoma 16a-hidroksiprednizolono reakcija su butanaliu acetonitrile. Kaip katalizatoriaus įdedama p-tolueno sulforūgšties. Reakcijos mišinys skiedžiamas vandeniu bei vandeniniu natrio hidrokarbonato tirpalu. Ataušinus iki 5-15°C, kristalizuotas produktas nufiltruojamas ir plaunamas vandeniu. Po to drėgna arba išdžiovinta medžiaga ištirpinama metileno chloride. Jeigu buvo naudojama drėgna medžiaga, pašalinama skiedimo metu susidariusi vandeninė fazė. Įdedama metanolio ir susidaręs nevalytas budezonidas nusodinamas, tuo tikslu įpilant ligroino arba kitokio tinkamo angliavandenilio (pvz., heksano, heptano ar cikloheksano), kuris po to nufiltruojamas.
Etapas. Budezonidas.
Nuvalytas budezonidas ištirpinamas metanolyje maždaug 60°C temperatūroje. Tirpalas nufiltruojamas pro tankų filtrą ir atliekamas produkto kristalizavimas, tuo tikslu įpilant vandens. Po aušinimo iki 520°C, filtravimo ir plovimo metanoliu/vandeniu budezonidas džiovinamas vakuume 40-45°C temperatūroje.
Palyginus su iki šiol žinomais procesais, šis yra paprastesnis, ekonomiškesnis ir mažiau pavojingas sveikatai.
Darbinis pavyzdys
Reakcija vykdoma azote. 15,4 g p-tolueno sulforūgšties ištirpinama 200 ml acetonitrilo. Į šį tirpalą įpilama 50,0 g 16a-dihidroksiprednizolono ir
17,6 g butanalio. Temperatūra pakyla iki 25°C. Per 30 min. didžioji medžiagos dalis ištirpsta. Netrukus po to produktas pradeda kristalizuotis. Po 3 valandų reakcija nutraukiama, įpilama 75 ml vandeninio prisotinto natrio hidrokarbonato tirpalo ir tada prasideda produkto kristalizacija. Išdžiovintas produktas ištirpinamas metileno chloride ir metanolyje ir kristalizuojamas, tuo tikslu įpilant ligroino (barometrinis slėgis - 40-65). Susidaro grynas budezonidas.
Nuvalytas budezonidas perkristalinamas iš metanolio vandens. Gaunamas grynas budezonidas su izomerų santykiu A:B 1:1 (aukšto slėgio skysčių chromatografija), [a]25 100-0° (c = 0,2; CH2CI2); M+430 (teoriškai 430,5).

Claims (3)

  1. Apibrėžtis
    1. (22 R,S)-16a, 17a-butilidendioksi-11 β, 21-dihidroksipregna1,4-dien-3,20-diono
    CH2OH ch2ch2ch2
    H (i) gavimo būdas, kurio metu 11 β, 16α, 17α, 21-tetrahidroksipregna 1,4-dien3,20-dionas ch2oh tirpiklyje dalyvaujant katalizatoriui reaguoja su butanaliu CH3CH2CH2CHO, besiskiriantis tuo, kad reakcija vyksta acetonitrile, katalizatoriumi naudojant p-tolueno sulforūgštį.
  2. 2. Gavimo būdas pagal 1 punktą, besiskiriantis tuo, kad reakcija nutraukia, įpilant vandens ir pakoreguojant reakcijos mišinio pH.
  3. 3. Gavimo būdas pagal 1 arba 2 punktą, besiskiriantis tuo kad reakcijai baigiantis susidarantys kristalai nufiltruojami, ištirpinami metileno chloride ir metanolyje, o po to kristalizuojami, tuo tikslu įpilant tinkamo angliavandenilio, tokio kaip ligroinas, heksanas, cikloheksanas ar heptanas ir susidaro nevalytas produktas, kuris po to perkristalinamas metanolyje/vandenyje ir gaunamas grynas budezonidas.
LTIP1729A 1989-10-02 1993-12-30 Process for the manufacture of budesonide LT3697B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE8903219A SE8903219D0 (sv) 1989-10-02 1989-10-02 Process for the manufacture of budesonide

Publications (2)

Publication Number Publication Date
LTIP1729A LTIP1729A (en) 1995-07-25
LT3697B true LT3697B (en) 1996-02-26

Family

ID=20377019

Family Applications (1)

Application Number Title Priority Date Filing Date
LTIP1729A LT3697B (en) 1989-10-02 1993-12-30 Process for the manufacture of budesonide

Country Status (25)

Country Link
US (1) US5556964A (lt)
EP (1) EP0494942B1 (lt)
JP (1) JP2965352B2 (lt)
KR (1) KR0160527B1 (lt)
AT (1) ATE130310T1 (lt)
AU (1) AU632864B2 (lt)
BG (1) BG61608B1 (lt)
BR (1) BR9007700A (lt)
CA (1) CA2065861C (lt)
CY (1) CY2084B1 (lt)
DE (1) DE69023664T2 (lt)
DK (1) DK0494942T3 (lt)
ES (1) ES2079491T3 (lt)
FI (1) FI103204B (lt)
HK (1) HK52097A (lt)
HU (1) HU212576B (lt)
LT (1) LT3697B (lt)
LV (1) LV10283B (lt)
NO (1) NO178827C (lt)
RO (1) RO110947B1 (lt)
RU (1) RU2048472C1 (lt)
SE (1) SE8903219D0 (lt)
SG (1) SG43344A1 (lt)
UA (1) UA26860C2 (lt)
WO (1) WO1991004984A1 (lt)

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SE9704186D0 (sv) * 1997-11-14 1997-11-14 Astra Ab New composition of matter
US6266556B1 (en) 1998-04-27 2001-07-24 Beth Israel Deaconess Medical Center, Inc. Method and apparatus for recording an electroencephalogram during transcranial magnetic stimulation
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US6883516B2 (en) 2000-04-27 2005-04-26 Chrysalis Technologies Incorporated Method for generating an aerosol with a predetermined and/or substantially monodispersed particle size distribution
US6491233B2 (en) 2000-12-22 2002-12-10 Chrysalis Technologies Incorporated Vapor driven aerosol generator and method of use thereof
US6501052B2 (en) 2000-12-22 2002-12-31 Chrysalis Technologies Incorporated Aerosol generator having multiple heating zones and methods of use thereof
US6681998B2 (en) 2000-12-22 2004-01-27 Chrysalis Technologies Incorporated Aerosol generator having inductive heater and method of use thereof
US7077130B2 (en) 2000-12-22 2006-07-18 Chrysalis Technologies Incorporated Disposable inhaler system
US6701921B2 (en) 2000-12-22 2004-03-09 Chrysalis Technologies Incorporated Aerosol generator having heater in multilayered composite and method of use thereof
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US20030055026A1 (en) 2001-04-17 2003-03-20 Dey L.P. Formoterol/steroid bronchodilating compositions and methods of use thereof
US6568390B2 (en) 2001-09-21 2003-05-27 Chrysalis Technologies Incorporated Dual capillary fluid vaporizing device
US6640050B2 (en) 2001-09-21 2003-10-28 Chrysalis Technologies Incorporated Fluid vaporizing device having controlled temperature profile heater/capillary tube
US6804458B2 (en) 2001-12-06 2004-10-12 Chrysalis Technologies Incorporated Aerosol generator having heater arranged to vaporize fluid in fluid passage between bonded layers of laminate
US6681769B2 (en) 2001-12-06 2004-01-27 Crysalis Technologies Incorporated Aerosol generator having a multiple path heater arrangement and method of use thereof
US6701922B2 (en) 2001-12-20 2004-03-09 Chrysalis Technologies Incorporated Mouthpiece entrainment airflow control for aerosol generators
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Also Published As

Publication number Publication date
BG61608B1 (bg) 1998-01-30
JPH05500669A (ja) 1993-02-12
HK52097A (en) 1997-05-02
EP0494942B1 (en) 1995-11-15
AU632864B2 (en) 1993-01-14
RU2048472C1 (ru) 1995-11-20
NO921233D0 (no) 1992-03-30
FI921426A0 (fi) 1992-04-01
AU6530990A (en) 1991-04-28
SG43344A1 (en) 1997-10-17
FI103204B1 (fi) 1999-05-14
BG96166A (bg) 1993-12-24
ATE130310T1 (de) 1995-12-15
BR9007700A (pt) 1992-08-11
HUT60281A (en) 1992-08-28
EP0494942A1 (en) 1992-07-22
NO178827C (no) 1996-06-12
HU212576B (en) 1996-08-29
LTIP1729A (en) 1995-07-25
ES2079491T3 (es) 1996-01-16
CA2065861A1 (en) 1991-04-03
NO178827B (no) 1996-03-04
LV10283B (en) 1995-04-20
RO110947B1 (ro) 1996-05-30
FI921426L (fi) 1992-04-01
WO1991004984A1 (en) 1991-04-18
UA26860C2 (uk) 1999-12-29
KR0160527B1 (ko) 1998-11-16
US5556964A (en) 1996-09-17
DK0494942T3 (da) 1996-03-11
LV10283A (lv) 1994-10-20
DE69023664T2 (de) 1996-05-02
SE8903219D0 (sv) 1989-10-02
CY2084B1 (en) 1998-10-16
FI103204B (fi) 1999-05-14
DE69023664D1 (de) 1995-12-21
JP2965352B2 (ja) 1999-10-18
HU9201064D0 (en) 1992-06-29
NO921233L (no) 1992-03-30
CA2065861C (en) 2001-06-05

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