AP582A - Pharmaceuticals - Google Patents

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Publication number
AP582A
AP582A APAP/P/1995/000730A AP9500730A AP582A AP 582 A AP582 A AP 582A AP 9500730 A AP9500730 A AP 9500730A AP 582 A AP582 A AP 582A
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AP
ARIPO
Prior art keywords
formula
compound
amino
preparation
chloro
Prior art date
Application number
APAP/P/1995/000730A
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AP9500730A0 (en
Inventor
John Robert Mansfield Dales
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Novartis Int Pharmaceutical Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D473/00Heterocyclic compounds containing purine ring systems

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Saccharide Compounds (AREA)
  • Chemical Treatment Of Metals (AREA)

Abstract

A process for the preparation of antiviral pirine derivatives proceeding via

Description

PHARMACEUTICALS
This invention relates to a process for the preparation of pharmaceutical 5 compounds.
The compound 2-amino-6-chloropurine (ACP) of formula:
NH2 is a useful intermediate in the preparation of nucleoside analogue antiviral agents, such as penciclovir (previously known as BRL 39123) and famciclovir (previously known as BRL 42810), described in EP-A-141927 (Example 1) and EP-A-182024 (Example 2), respectively. The intermediate is 9-substituted with an appropriate side chain precursor, followed by conversion of the 6-chloro moiety to a hydroxy (a guanine) or hydrogen (a 2-aminopurine).
A process from ACP is generally described in EP-A-302644 and US Patent No 5175288 and an improved process over the process specifically described in this 3 publication has now been discovered. The key difference is that in the original process the 3 chlorine group in the 6-position of the purine molecule is removed early in the process (see tr reaction Scheme 1). Significant yield and processing advantages are obtained by retaining the 6-chloro substituent in the molecule through the process, removing it only at the final step (see reaction Scheme 2). With streamlining of the process stages and removal of the c column chromatography steps, which would have rendered the route disadvantageous as a production process, overall yields have been increased from 10.6% to 41%. c
Accordingly, the present invention provides a process for the preparation of c penciclovir/famciclovir from ACP which process comprises the process from ACP as described in EP-302644, characterised in that the 6-chloro substituent is removed subsequent to the decarboxylation and hydrolysis steps.
As no aqueous dilution is used to precipitate the product at the coupling step there is large capacity advantage, and the dimethylformamide is more easily recovered as it does not have to be separated from a large volume of w ater.
There are greater overall volume efficiencies in the process.
The following Examples illustrate the invention.
- 1 P3O92O
AP.η η 5 8 2
EXAMPLE 1 (Stage 1 Product)
Preparation of 2-amino-6-chIoro-9-(methyl 2-carbomethoxybutanoate-4-yl)purine
A mixture of 2-amino-6-chloropurine (9.18g, 53.1 mmole), triethyl 3-bromopropane5 1,1,1-tricarboxyIate (20.33g, 57.3 mmole), potassium carbonate (1 l.lg, 80.3 mmole) and dimethylformamide (190ml) were stirred together at 60°C to 63°C for 22h. After this time the reaction mixture was filtered hot through a celite bed and the cake washed with dimethylformamide (30ml). The filtrate and washing were combined and the solvent removed under high vacuum distillation to leave a crude reddish brown oil. This was dissolved in methanol (140ml), cooled to 20°C and then a solution of sodium methoxide (1,2g) in methanol (40ml) was added with stirring. After ca 20 minutes a precipitate formed and the stirring was continued for a total of 1 hour. The reaction mixture was then cooled to 15°C and held at this temperature for 30 minutes. The product was filtered off and washed with methanol (10ml) and dried at 40°C for 16h under vacuum.
Yield: 12.0g of 95% purity material.
ΛΡ/Ρ/ y 5 / 'j υ /
AP. Ο Π 5 8 2
P30920
EXAMPLE 2 (Stage 2 product)
Preparation of 9-(4-acetoxy-3-acetoxjTnethylbut-l-yl)-2-amino-6-chIoropurine
A mixture of 2-amino-6-chloro-9-(methyl 2-carbomethoxybutanoate-4-yl) purine (32.7g, 0.1 mole), sodium borohydride (11.5g, 0.3 mole) and methylene dichloride (125ml) were stirred at 20°C. Methanol (75ml) was added dropwise over 2.0 hour period while the reaction temperature was maintained at 20-22°C with cooling. The reaction mixture was left to stir for a further 1.5h. Water (100ml) was added followed by the dropwise addition of concentrated hydrochloric acid (20-22ml) to pH 6.7 to 7.0 keeping the reaction temperature at 20°-22°C. Methylene dichloride and methanol were removed under vacuum until a reaction volume of 150ml was obtained. The reaction mixture was cooled to 5°C and stirred at this temperature for 30 minutes. The resulting precipitate was filtered off and the product cake washed with cold water (20ml). The resulting damp solid (4050g) was stirred with triethylamine (15ml), 4-dimethylaminopyridine (l.Og) in methylene dichloride (250ml). Acetic anhydride (75ml, 0.79 mole) was added dropwise over 20 to 30 minutes at such a rate to control the reflux. The reaction mixture was heated under reflux for a further 1.5 hours. The reaction was cooled to 20°C and neutralised with 20% w/w sodium hydroxide solution to pH 6.4-6.5. The methylene dichloride layer was separated and the aqueous phase extracted with methylene dichloride (100ml). The combined methylene dichloride phases were evaporated to dryness. The crude damp solid was recrystallised from 3:1 methanobwater (75ml), cooling the precipitate to -5°C for lh before filtration. The product was washed with cold 3:1 methanobwater (0°C) and dried at 40°C for 16h in a vacuum oven.
Yield: 23g of 97% to 98% purity material
-3P30920
AJ^ . ·.· / 3 β έ
EXAMPLE 3 (Stage 3 Product)
a) Preparation of 9-(4-acetoxy-3-acetoxymethyIbut-l-y!)-2-aminopurine - famciclovir
A mixture of 9-(4-acetoxy-3-acetoxyrnethylbut-l-yl)-2-amino-6-chloropurine (15.4g, 43 mmole), 5% palladium on carbon (6.16g), triethylamine (6.6ml, 47 mmole) and ethyl acetate (77ml) was stirred at 50°C under a hydrogen atmosphere at 1 bar pressure in an autoclave for 3 to 5 hours. After completion of the reaction the mixture was removed from the autoclave which was washed out with ethyl acetate (30ml) keeping the washings at 50°C. The main reaction mixture was filtered through a celite bed followed by the washings and finally with ethyl acetate (30ml). Water (46ml) was added to the combined ethyl acetate filtrate plus washings. The ethyl acetate was evaporated to dryness to leave a crude white solid. This was recrystallised from n-butanol (62ml), stirring the cooled solution at 0 to 5°C for 3h before filtration. The product was filtered off and washed with the mother liquors. The solid was reslurried in n-heptane (50ml) stirred for 30 minutes and filtered. The product was dried at 40°C for 16h under vacuum.
Yield; ll-11.3g
b) Preparation of 9-(4-hydroxy-3-hydroxymethylbut-l-yl) guanine - pencidovir
A mixture of 9-(4-acetoxy-3-acetoxymethylbut-l-yl)-2-amino-6-chloropurine (lOg,
28.1mmole), formic acid (96%, 6.3ml) and water (55ml) was stirred and heated to reflux for about 4 hours. After cooling the solution was basified by mixing with sodium hydroxide solution (12.5M, 27ml) and the resulting solution was stirred for 1.5 hrs. The solution was neutralised by the addition of formic acid. The resultant sluny was heated to reflux (pa 105°C) then cooled to 40 - 45°C and stirred for about 3 hours. The crude product is then isolated and washed with water (20ml). The isolated product was dissolved in sodium hydroxide solution (3M, 80ml). Carbon (ca 1.5g) was added and the slurry stirred for about 1 hr then the carbon was removed by filtration and w ashed with water (20ml). The solution was neutralised by the addition of formic acid and the resultant precipitate was redissolved by heating to pa 100°C and was then cooled. The precipitated product was stirred for about 3 hrs then isolated and washed with water (2 x 20ml) before being dried.
>
X
X
CC un
O
O
Yield 5.3 - 5.5g.
- 4 Mi*
Process of EP-A-30P644
V
Process of the Invention
L «Λ V‘ 4J·
A process for the preparation of a compound of formula (A):

Claims (9)

  1. Claims (CHJ
  2. 2'2
    RaO-CH2-CH-CH2-ORb (A) wherein:
    X is hydrogen, hydroxy, chloro, Cj.g alkoxy or phenyl Cj.g alkoxy; and Ra and Rg are 10 hydrogen, or acyl or phosphate derivatives thereof, which process comprises:
    (i) the preparation of a compound of formula (I):
    0)
    AF/F/ 95/ 00730 wherein Rj is Cpg alkyl, or phenyl C^.g alkyl in which the phenyl group is optionally substituted; R2 is hydrogen, hydroxy, chlorine, Cpg alkoxy, phenyl Cj.g alkoxy or amino; and R3 is halogen, alkylthio, Cj.g alkylsulphonyl, azido, an amino group or a
    20 protected amino group, which preparation comprises the reaction of a compound of formula (Π):
    (II)
    P30920 ak . ν υ δ ' wherein R2 and R3 are as defined for formula (I) with:
    a compound of formula (V):
    L-(CH2)-C— co2r, oo2r, (V) wherein L is a leaving group and Rj is as defined for formula (I), to give a compound of formula (VI):
    I (CH2)2
    Ri co2r, (VI) and thereafter converting the intermediate compound of formula (VI) to a compound of 15 formula (I) via decarboxylation, and, as necessary or desired, interconverting variables Rj,
    R2 and R3 to further values of Rj, R2 and R3;
    cr (ii) the conversion of the resulting compound of formula (I) to a compound of formula (A) by converting variable R3, when other than amino, to amino, reducing the ester groups
    20 CO2R} to CH2OH and optionally forming acyl or phosphate derivatives thereof, and as necessary or desired converting variable R2 in the compound of formula (I) to variable X in the compound of formula (A);
    characterised in that
    R2 is chloro in formula (I).
    ,'Ρ?092ύ
    AP . 0 0 5 8 2
    2. A process for the preparation of a compound of formula (I) as defined in claim 1, which process comprises the reaction of a compound of formula (II) wherein R2 and R3 are as defined in claim 1 with a compound of formula (V) wherein Rj is C1.4 alkyl and L is halogen, followed by decarboxylation of the resulting compound of formula (VI), and, as necessary or desired, interconverting Rj, R2 and R3 in the resulting compound of formula (I) to further values of Rj, R2 and R3 as defined for formula (I) in claim 1.
  3. 3. A compound of formula (I) wherein R2 is chloro, or a salt thereof:
    ί 10 wherein Rj, R2 and R3 are as defined in claim 1.
  4. 4. A compound according to claim 3 or a salt thereof, wherein R| is methyl or ethyl and R3 is amino.
  5. 5. 2- Amino-6-chloro-9- (methyl 2-carbomethoxybutanoate-4-yl)purine.
  6. 6. A process according to Claim 1 for the preparation of 9-(4-acetoxy-3acetoxymethylbut-l-yl)-2-aminopurine (famciclovir).
  7. 7. A process according to claim 1 for the preparation of 9-(4-hydroxy-3hydroxymethylbut-l-yl)guanine (penciclovir).
    AP/P/ 9 5 / 0 0 7 3 0
    P30920
    Λ ρ λ η α ρ ο
  8. 8. A process for the preparation of famciclovir from 2-amino-6-chloropurine (ACP) which process comprises the process from ACP as described in EP-A-302644, characterised in that the 6-chloro substituent is removed subsequent to the decarboxylation and hydrolysis steps.
  9. 9. A process for the preparation of penciclovir from 2-amino-6-chloropurine (ACP) which process comprises the process from ACP as described in EP-A-302644, characterised in that the 6-chloro substituent is removed subsequent to the decarboxylation and hydrolysis steps.
APAP/P/1995/000730A 1994-04-19 1995-04-13 Pharmaceuticals AP582A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB9407698A GB9407698D0 (en) 1994-04-19 1994-04-19 Pharmaceuticals

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AP9500730A0 AP9500730A0 (en) 1995-04-30
AP582A true AP582A (en) 1997-04-09

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APAP/P/1995/000730A AP582A (en) 1994-04-19 1995-04-13 Pharmaceuticals
APAP/P/1996/000870A AP703A (en) 1994-04-19 1995-04-19 Preparation of purines.

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US (2) US6846927B1 (en)
EP (1) EP0756597B1 (en)
JP (1) JP3936734B2 (en)
KR (1) KR100327147B1 (en)
CN (1) CN1045963C (en)
AP (2) AP582A (en)
AT (1) ATE201209T1 (en)
AU (1) AU691000B2 (en)
BG (1) BG63464B1 (en)
BR (1) BR9507494A (en)
CA (1) CA2188181C (en)
CZ (1) CZ287674B6 (en)
DE (1) DE69520945T2 (en)
DK (1) DK0756597T3 (en)
DZ (1) DZ1872A1 (en)
EG (1) EG20938A (en)
ES (1) ES2158948T3 (en)
FI (1) FI119691B (en)
GB (1) GB9407698D0 (en)
GR (1) GR3036338T3 (en)
HK (1) HK1012348A1 (en)
HU (1) HU226209B1 (en)
IL (1) IL113409A (en)
IN (1) IN183830B (en)
MA (1) MA23518A1 (en)
MX (1) MX9604942A (en)
MY (1) MY128846A (en)
NO (1) NO315000B1 (en)
NZ (1) NZ287858A (en)
OA (1) OA10376A (en)
PL (1) PL181219B1 (en)
PT (1) PT756597E (en)
RO (1) RO118950B1 (en)
RU (1) RU2158266C2 (en)
SA (1) SA95150619B1 (en)
SK (1) SK283193B6 (en)
TW (1) TW311138B (en)
UA (1) UA47401C2 (en)
WO (1) WO1995028402A2 (en)
ZA (1) ZA953110B (en)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9615253D0 (en) * 1996-07-20 1996-09-04 Smithkline Beecham Plc Pharmaceuticals
GB9615276D0 (en) * 1996-07-20 1996-09-04 Smithkline Beecham Plc Pharmaceuticals
GB9807116D0 (en) 1998-04-02 1998-06-03 Smithkline Beecham Plc Novel process
GB9807114D0 (en) * 1998-04-02 1998-06-03 Smithkline Beecham Plc Novel process
WO2004018470A2 (en) * 2002-08-26 2004-03-04 Teva Pharmaceutical Industries Ltd. Crystalline solid famciclovir forms i, ii, iii and preparation thereof
TW200510415A (en) * 2003-04-30 2005-03-16 Teva Pharma Process for the preparation of famciclovir
US20050143400A1 (en) * 2003-09-04 2005-06-30 Genny Shamai Process for preparing famciclovir
US7458839B2 (en) * 2006-02-21 2008-12-02 Fci Americas Technology, Inc. Electrical connectors having power contacts with alignment and/or restraining features
US20050215787A1 (en) * 2004-03-26 2005-09-29 Joshi Ramesh A An improved process for the preparation of purines
WO2005116031A1 (en) * 2004-05-18 2005-12-08 Teva Pharmaceutical Industries Ltd. Drying process for preparing crystalline solid famciclovir
GB2426247A (en) * 2005-05-20 2006-11-22 Arrow Int Ltd Methods of preparing purine derivatives such as famciclovir
CN102070636B (en) * 2011-01-17 2012-05-23 浙江大学 Preparation method of penciclovir
CN104086552B (en) * 2014-07-31 2016-01-13 济南兆康医药科技有限公司 A kind of process for purification of Penciclovir
CN104496991A (en) * 2014-11-04 2015-04-08 常州康丽制药有限公司 Preparation method for high-quality 2-amino-6-chloro-9-(4-hydroxy-3-hydroxymethylbutyl)purine
CN104744472A (en) * 2015-03-12 2015-07-01 常州康丽制药有限公司 Preparation method of high-quality 2-amino-6-chloro-9-(4-hydroxyl-3-hydroxymethylbutyl) purine
CN108314685B (en) * 2018-03-16 2020-08-25 上药康丽(常州)药业有限公司 Preparation method of 2-amino-6-chloro-9- (4-acetoxyl-3-acetoxymethyl butyl) purine
CN110713490A (en) * 2018-07-12 2020-01-21 浙江医药股份有限公司新昌制药厂 Preparation method of penciclovir

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0141927A2 (en) * 1983-08-18 1985-05-22 Beecham Group Plc Antiviral guanine derivatives
EP0302644A2 (en) * 1987-08-01 1989-02-08 Beecham Group Plc Purine compounds and their preparation
EP0352953A2 (en) * 1988-07-23 1990-01-31 Beecham Group Plc Process for the preparation of purine derivatives
EP0369583A1 (en) * 1988-09-21 1990-05-23 Beecham Group Plc Chemical process for the preparation of purine derivatives

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0182024B1 (en) * 1984-09-20 1991-04-03 Beecham Group Plc Purine derivatives and their pharmaceutical use

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0141927A2 (en) * 1983-08-18 1985-05-22 Beecham Group Plc Antiviral guanine derivatives
EP0302644A2 (en) * 1987-08-01 1989-02-08 Beecham Group Plc Purine compounds and their preparation
EP0352953A2 (en) * 1988-07-23 1990-01-31 Beecham Group Plc Process for the preparation of purine derivatives
EP0369583A1 (en) * 1988-09-21 1990-05-23 Beecham Group Plc Chemical process for the preparation of purine derivatives

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FI964193A0 (en) 1996-10-18
NZ287858A (en) 1998-06-26
CN1045963C (en) 1999-10-27
EP0756597B1 (en) 2001-05-16
GB9407698D0 (en) 1994-06-15
AP9500730A0 (en) 1995-04-30
EG20938A (en) 2000-06-28
MA23518A1 (en) 1995-12-31
SK283193B6 (en) 2003-03-04
KR100327147B1 (en) 2002-07-27
TW311138B (en) 1997-07-21
MY128846A (en) 2007-02-28
DK0756597T3 (en) 2001-08-20
DE69520945T2 (en) 2002-03-28
CZ287674B6 (en) 2001-01-17
OA10376A (en) 2001-11-20
BG63464B1 (en) 2002-02-28
PL181219B1 (en) 2001-06-29
FI964193A (en) 1996-12-18
AU2670695A (en) 1995-11-10
BR9507494A (en) 1997-08-12
FI119691B (en) 2009-02-13
AP703A (en) 1998-12-04
CA2188181A1 (en) 1995-10-26
UA47401C2 (en) 2002-07-15
HK1012348A1 (en) 1999-07-30
MX9604942A (en) 1998-05-31
HUT75339A (en) 1997-05-28
DE69520945D1 (en) 2001-06-21
WO1995028402A3 (en) 1996-01-25
JP3936734B2 (en) 2007-06-27
SA95150619B1 (en) 2005-05-04
PL316943A1 (en) 1997-02-17
RU2158266C2 (en) 2000-10-27
SK133296A3 (en) 1997-05-07
RO118950B1 (en) 2004-01-30
IL113409A0 (en) 1995-07-31
NO964395D0 (en) 1996-10-15
CN1150427A (en) 1997-05-21
AP9600870A0 (en) 1996-10-31
EP0756597A1 (en) 1997-02-05
ATE201209T1 (en) 2001-06-15
US6846927B1 (en) 2005-01-25
KR970702280A (en) 1997-05-13
US20050101570A1 (en) 2005-05-12
NO964395L (en) 1996-10-15
HU226209B1 (en) 2008-06-30
ES2158948T3 (en) 2001-09-16
CA2188181C (en) 2007-04-17
HU9602891D0 (en) 1996-12-30
CZ305396A3 (en) 1997-06-11
WO1995028402A2 (en) 1995-10-26
IN183830B (en) 2000-04-29
AU691000B2 (en) 1998-05-07
ZA953110B (en) 1996-05-20
NO315000B1 (en) 2003-06-23
US7355043B2 (en) 2008-04-08
IL113409A (en) 1999-08-17
GR3036338T3 (en) 2001-11-30
PT756597E (en) 2001-11-30
BG100926A (en) 1997-07-31
DZ1872A1 (en) 2002-02-17
JPH09512000A (en) 1997-12-02

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