KR20040107647A - Process for preparing intermediate of simvastatin - Google Patents

Process for preparing intermediate of simvastatin Download PDF

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KR20040107647A
KR20040107647A KR1020030036671A KR20030036671A KR20040107647A KR 20040107647 A KR20040107647 A KR 20040107647A KR 1020030036671 A KR1020030036671 A KR 1020030036671A KR 20030036671 A KR20030036671 A KR 20030036671A KR 20040107647 A KR20040107647 A KR 20040107647A
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formula
simvastatin
alcohol solvent
preparing
lovastatin
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KR1020030036671A
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Korean (ko)
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권웅
이재형
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주식회사 삼오제약
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Publication of KR20040107647A publication Critical patent/KR20040107647A/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K1/00Lift valves or globe valves, i.e. cut-off apparatus with closure members having at least a component of their opening and closing motion perpendicular to the closing faces
    • F16K1/16Lift valves or globe valves, i.e. cut-off apparatus with closure members having at least a component of their opening and closing motion perpendicular to the closing faces with pivoted closure-members
    • F16K1/18Lift valves or globe valves, i.e. cut-off apparatus with closure members having at least a component of their opening and closing motion perpendicular to the closing faces with pivoted closure-members with pivoted discs or flaps
    • F16K1/22Lift valves or globe valves, i.e. cut-off apparatus with closure members having at least a component of their opening and closing motion perpendicular to the closing faces with pivoted closure-members with pivoted discs or flaps with axis of rotation crossing the valve member, e.g. butterfly valves
    • F16K1/226Shaping or arrangements of the sealing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K1/00Lift valves or globe valves, i.e. cut-off apparatus with closure members having at least a component of their opening and closing motion perpendicular to the closing faces
    • F16K1/32Details
    • F16K1/34Cutting-off parts, e.g. valve members, seats
    • F16K1/36Valve members
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K1/00Lift valves or globe valves, i.e. cut-off apparatus with closure members having at least a component of their opening and closing motion perpendicular to the closing faces
    • F16K1/32Details
    • F16K1/34Cutting-off parts, e.g. valve members, seats
    • F16K1/46Attachment of sealing rings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K27/00Construction of housing; Use of materials therefor
    • F16K27/02Construction of housing; Use of materials therefor of lift valves
    • F16K27/0209Check valves or pivoted valves
    • F16K27/0218Butterfly valves

Abstract

PURPOSE: A process for preparing an intermediate of simvastatin is provided, thereby stably carrying out hydrolysis of lovastatin under the strong basic condition by using a mixed solvent and cheaply and industrially preparing the intermediate of simvastatin which is useful as a HMG-CoA reductase inhibitor. CONSTITUTION: The process for preparing an intermediate of simvastatin, 6(R)-(2-(8'(S)-hydroxy-2'(S), 6'(R)-dimethyl-1',2',6',7',8',8'a(R)- hexahydronaphthyl-1'(S))-ethyl)- 4(R)-hydroxy-3,4,5,6-tetrahydro-2H-pyran-2-one of the formula(I), comprises the steps of: hydrolyzing lovastatin of the formula(III) in the presence of inorganic base in a mixed alcohol solvent of tetrahydrofuran and alcohol selected from primary, secondary or tertiary alcohol solvent to prepare triol acid of the formula(II); and acidifying or lactonizing the triol acid of the formula(II), wherein the primary alcohol solvent is normal propanol or normal butanol; the secondary alcohol solvent is isopropanol or isobutanol; and tertiary alcohol solvent is t-butanol.

Description

심바스타틴의 중간체 화합물의 제조방법{Process for preparing intermediate of simvastatin}Process for preparing intermediate compound of simvastatin {Process for preparing intermediate of simvastatin}

본 발명은 고콜레스테롤 혈증 치료제로 유용한 심바스타틴의 중간체 화합물을 제조하는 방법에 관한 것으로, 상세하게는 하기 구조식(Ⅰ)의 6(R)-[2-(8'(S)-히드록시-2'(S),6'(R)-디메틸-1',2',6',7',8',8'a(R)-헥사히드로나프틸-1'(S))-에틸]-4(R)-히드록시-3,4,5,6-테트라히드로-2H-피란-2-온(디올 락톤)의 제조방법에 관한 것이다.The present invention relates to a method for preparing an intermediate compound of simvastatin useful as a therapeutic agent for hypercholesterolemia, and specifically, 6 (R)-[2- (8 '(S) -hydroxy-2' of the following structural formula (I). (S), 6 '(R) -Dimethyl-1', 2 ', 6', 7 ', 8', 8'a (R) -hexahydronaphthyl-1 '(S))-ethyl] -4 A method for producing (R) -hydroxy-3,4,5,6-tetrahydro-2H-pyran-2-one (diol lactone).

심바스타틴은 HMG-CoA 리덕타제 억제제로서 콜레스테롤의 생합성을 저해하는 물질로 고콜레스테롤 혈증 치료제로서 알려져있다.Simvastatin is an HMG-CoA reductase inhibitor and a substance that inhibits the biosynthesis of cholesterol and is known as a drug for hypercholesterolemia.

심바스타틴을 제조하기 위한 출발물질로는 아스페르길루스(Aspergillus) 속에 속하는 미생물 주를 사용한 발효 공정을 통하여 제조가능한 하기 구조식(Ⅲ)의 로바스타틴을 사용할 수 있다(미국 특허 제 4,444,784호).As a starting material for preparing simvastatin, lovastatin of the following structural formula (III) which can be prepared through a fermentation process using a microorganism strain belonging to the genus Aspergillus (US Pat. No. 4,444,784) can be used.

지금까지 알려진 바로는, 최종 목적물질인 심바스타틴의 제조에 유용한 중간체인 구조식(I)의 디올 락톤에 대한 제조기술은 하기 반응식 1에서와 같은 과정을 거쳐 제조되는 것으로 알려져 있다.To date, it is known that the preparation technique for the diol lactone of the structural formula (I), which is an intermediate useful for preparing the final target substance simvastatin, is prepared through the same process as in Scheme 1 below.

미국 특허 제 4,444,784호는 상기 구조식(Ⅲ)의 로바스타틴을 수산화리튬으로 가수분해하여 구조식(Ⅱ)의 트리올산을 얻고, 이를 락톤화시켜 구조식(Ⅰ)의 디올 락톤을 얻는 방법을 개시하고 있다.U.S. Patent No. 4,444,784 discloses a method of hydrolyzing lovastatin of formula (III) with lithium hydroxide to obtain triol acid of formula (II) and lactonizing to obtain diol lactone of formula (I).

그러나 상기한 종래 방법은 상기 구조식(Ⅱ)의 제조(가수분해반응)시 과량의 물 용매(로바스타틴 대비 75배)에서 장시간(12 내지 56시간), 고온(100 내지 130℃) 및 가압조건하에서 수행되어야만 하는 단점을 갖고 있고, 이로 인한 부생성물이 생성되며 수율(81%)도 낮음으로서 비효율적인 생산방법이다.However, the above-mentioned conventional method is carried out under a long time (12 to 56 hours), high temperature (100 to 130 ° C.) and pressurized conditions in an excess water solvent (75 times compared to lovastatin) during the preparation of the structural formula (II) (hydrolysis reaction). It has disadvantages that must be made, and by-products are generated and yield is low (81%), which is an inefficient production method.

보다 더 개량된 방법으로 한국 특허 공개번호 제 10-2001-0040760호(우선권 주장 일본특허 제 98-531865호)에 의하면 구조식(Ⅲ)의 로바스타틴을 질소 기체와 같은 불활성 대기에서 과량의 2차 또는 3차 알콜 용매(로바스타틴 대비 12 내지 40배)를 사용, 무기염기로 가수분해하여 구조식(Ⅱ)의 트리올산을 얻고, 이를 락톤화반응시켜 구조식(I)의 디올 락톤을 얻는 방법을 개시하고 있다.In a further improved method, according to Korean Patent Publication No. 10-2001-0040760 (priority claim Japanese Patent No. 98-531865), lovastatin of formula (III) is used in excess of secondary or 3 in an inert atmosphere such as nitrogen gas. A method of obtaining a diol lactone of the structural formula (I) by hydrolyzing with an inorganic base using a secondary alcohol solvent (12-40 times compared to lovastatin) to obtain a triol acid of the structural formula (II), and performing lactolation reaction.

그러나 이 방법도 또한 알콜 용매에 따라 장시간(1 내지 60시간) 및 고온(60내지 100℃)의 가혹한 반응조건이 요구되므로 부생성물이 생성되고 수율과 순도면에서 낮아 부적합한 생산방법이다.However, this method is also an unsuitable production method due to the severe reaction conditions of long time (1 to 60 hours) and high temperature (60 to 100 ° C.) depending on the alcohol solvent, resulting in by-products and low yield and purity.

본 발명자는 상기와 같은 문제점을 해결하고자 부단한 실험을 통해 디올락톤 중간체의 개선된 제조방법을 완성하여 출원하고자 한다.The present inventors intend to complete the improved manufacturing method of the diolactone intermediate through the uninterrupted experiment to solve the above problems.

따라서, 본 발명은 상기한 심바스타틴 제조시 파생되는 제반 문제점인 가수분해반응의 수율 및 순도를 개선함으로써 상업적으로나 경제적으로 유리한 구조식(I)의 디올 락톤 중간체를 제조하는 새로운 제조방법을 제공하고자 한다.Accordingly, the present invention is to provide a novel method for preparing a commercially and economically advantageous diol lactone intermediate of the formula (I) by improving the yield and purity of the hydrolysis reaction, which is a general problem derived from the preparation of simvastatin.

상기 목적을 달성하기 위하여, 본 발명은 구조식(Ⅲ)의 로바스타틴을 무기염기 존재하에 테트라히드로퓨란 및 1차, 2차 또는 3차 알콜용매로부터 선택된 1종이상의 알콜 혼합용매 중에서 반응시켜 가수분해를 수행함으로써, 하기 구조식(Ⅱ)의 트리올산을 고순도로 제조하는 제 1단계; 상기 트리올산을 산성화 및 락톤화반응시켜 구조식(I)의 디올 락톤인 6(R)-[2-(8'(S)-히드록시-2'(S),6'(R)-디메틸-1',2',6',7',8',8'a(R)-헥사히드로나프틸-1'(S))-에틸]-4(R)-히드록시-3,4,5,6-테트라히드로-2H-피란-2-온을 연속적으로 제조하는 제 2단계를 포함하는 심바스타틴 중간체의 제조방법을 제공한다.In order to achieve the above object, the present invention performs hydrolysis by reacting lovastatin of formula (III) in at least one alcohol mixed solvent selected from tetrahydrofuran and a primary, secondary or tertiary alcohol solvent in the presence of an inorganic base. Thereby, the first step of producing a triol acid of the structural formula (II) in high purity; The triol acid was acidified and lactonated to give 6 (R)-[2- (8 '(S) -hydroxy-2' (S), 6 '(R) -dimethyl-, which is a diol lactone of formula (I). 1 ', 2', 6 ', 7', 8 ', 8'a (R) -hexahydronaphthyl-1' (S))-ethyl] -4 (R) -hydroxy-3,4,5 Provided is a method for preparing a simvastatin intermediate comprising a second step of continuously preparing 6-tetrahydro-2H-pyran-2-one.

본 발명을 보다 구체적으로 설명하면 다음과 같다.The present invention will be described in more detail as follows.

상기 제 1단계에서 구조식(Ⅲ)의 로바스타틴을 테트라히드로퓨란 및 1차, 2차 또는 3차 알콜로부터 선택된 혼합용매 중에서 무기염기로 처리하여 가수분해시켜 구조식(Ⅱ)의 트리올산을 수득 가능하다.In the first step, lovastatin of formula (III) can be hydrolyzed by treatment with an inorganic base in a mixed solvent selected from tetrahydrofuran and primary, secondary or tertiary alcohols to obtain trioleic acid of formula (II).

상기 단계에서 알콜용매는 1차, 2차 또는 3차 알콜 모두 가능하며, 바람직하게는 탄소수가 3 내지 6의 알콜용매가 적당하고, 특별히 제한되지는 않지만 노말프로판올, 노말부탄올, 이소프로판올, 이소부탄올, t-부탄올 등이 바람직하며, 노말프로판올, 이소프로판올이 보다 바람직하다.In this step, the alcohol solvent may be a primary, secondary or tertiary alcohol, preferably an alcohol solvent having 3 to 6 carbon atoms is suitable, and is not particularly limited, but normal propanol, normal butanol, isopropanol, isobutanol, t-butanol and the like are preferable, and normal propanol and isopropanol are more preferable.

상기 단계에서 혼합용매의 사용량은 로바스타틴 대비 3 내지 5배, 바람직하게는 4배를 사용하고, 혼합용매의 비율 및 테트라히드로퓨란의 사용비는 0.5 내지 1.5:1가 바람직하며, 1 : 1의 비율로 사용하는 것이 보다 바람직하다.The amount of the mixed solvent used in this step is 3 to 5 times, preferably 4 times compared to lovastatin, the ratio of the mixed solvent and the ratio of tetrahydrofuran is preferably 0.5 to 1.5: 1, the ratio of 1: 1 It is more preferable to use as.

상기 단계에서, 반응온도는 60 내지 100℃, 바람직하게는 70 내지 90℃ 에서 수행되는 것이 바람직하며, 반응시간은 10분 내지 5시간, 바람직하게는 1 내지 3시간정도 반응시키는 것이 적합하다.In this step, the reaction temperature is preferably carried out at 60 to 100 ℃, preferably 70 to 90 ℃, the reaction time is suitable to react for 10 minutes to 5 hours, preferably 1 to 3 hours.

상기 단계에서, 무기염기는 특별히 제한되지는 않지만, 수산화리튬, 수산화나트륨, 수산화칼륨 등과 같은 알칼리금속 히드록사이드 및 칼륨 t-부톡시드, 나트륨 이소프로폭시드 등과 같은 알칼리금속 알콕시드, 가장 바람직하기로는 수산화칼륨이고, 상기 무기염기는 로바스타틴양에 대하여 5 내지 10 몰당량, 바람직하게는 6 내지 8 몰당량을 사용함이 바람직하다.In this step, the inorganic base is not particularly limited, but most preferably alkali metal hydroxides such as lithium hydroxide, sodium hydroxide, potassium hydroxide and the like and alkali metal alkoxides such as potassium t-butoxide, sodium isopropoxide and the like, most preferably Is potassium hydroxide, and the inorganic base is preferably 5 to 10 molar equivalents, preferably 6 to 8 molar equivalents, relative to the amount of lovastatin.

제 2단계는 제 1단계에서 얻어진 구조식(Ⅱ) 화합물을 락톤화시키기 위하여, 황산, 인산, 메탄술폰산 등과 같은 산으로, pH 3 내지 5, 바람직하게는 pH 3.5 산성화 조건하에서 톨루엔, 크실렌 등과 같은 불활성용매를 가하여 30분내지 3시간, 바람직하게는 1시간동안 환류교반함으로 목적하는 구조식(Ⅱ) 화합물을 수득할 수 있다.The second step is an acid such as sulfuric acid, phosphoric acid, methanesulfonic acid, and the like, in order to lactonate the compound of formula (II) obtained in the first step, and inert such as toluene, xylene, etc. The solvent can be added to reflux stirring for 30 minutes to 3 hours, preferably 1 hour, to obtain the desired compound of formula II.

통상적으로 구조식(Ⅱ)의 트리올산은 단리시키지 않으며 산성화된 반응 혼합물의 농축물 형태로 락톤화 반응을 거쳐 구조식(I)의 디올 락톤을 수득가능하고, 이 락톤화 반응은 통상적인 방법에 의하여 수행가능하며, 생성된 구조식(II)의 트리올산 및 구조식(I)의 디올 락톤 최종물질의 생성확인은 고성능 액체 크로마토그래피로 정성 및 정량적으로 측정하여 수율 및 순도를 계산 가능한데, 본 발명에 의한 제법은, 반응 중 트리올산의 순도는 97% 이상으로 종래의 방법이 제공하는 트리올산 순도인 85 내지 92% 보다 월등한 순도를 나타냈는데, 결과적으로 최종 분리 정제된 구조식(I)의 디올 락톤의 순도는 98.5%이상이며, 수율 또한 97% 이상으로 기존 방법의 수율인 80 내지 85% 보다 훨씬 탁월한 실험결과를 나타내었다.Typically triol acid of formula (II) is not isolated and can be obtained by lactonation in the form of a concentrate of the acidified reaction mixture to obtain diol lactone of formula (I), which is carried out by conventional methods. It is possible to confirm the production of the resulting triol acid of formula (II) and diol lactone final structure of formula (I) by qualitatively and quantitatively measuring by high performance liquid chromatography to calculate the yield and purity. In the reaction, the purity of triol acid was more than 97%, which was superior to that of 85 to 92% of the triol acid purity provided by the conventional method. As a result, the purity of the diol lactone of the final separated and purified formula (I) was The yield was more than 98.5%, the yield was also more than 97%, which was much better than the 80 to 85% yield of the conventional method.

이하 실시예를 통해 본 발명을 보다 상세하게 설명하기로 한다. 단, 이하의 실시예는 단지 본 발명의 바람직한 구체예를 제시하기 위한 것일 뿐, 그것에 의해본 발명의 범위가 제한되지 않는 것임은 물론이다. 본 발명은 이하의 실시예를 포함함은 물론, 본 발명의 기술적 사상의 범위를 일탈하지 않는 범위 내에서 다양한 개변예 및 수정예를 그 범위에 포함하는 것이다.Hereinafter, the present invention will be described in more detail with reference to the following examples. However, the following examples are only intended to present preferred embodiments of the present invention, and the scope of the present invention is not limited thereby. The present invention includes not only the following embodiments but also various modifications and modifications within the scope without departing from the scope of the technical idea of the present invention.

참조예. 고성능 액체크로마토그래피 분석조건Reference example. High performance liquid chromatography analysis conditions

본 발명의 화합물은 하기 조건하에서 고성능 액체 크로마토그래피로 정성 및 정량적으로 측정하였다.Compounds of the present invention were determined qualitatively and quantitatively by high performance liquid chromatography under the following conditions.

기구 : SCL-10A, 시마주사(Shimadzu Corporation)Organization: SCL-10A, Shimadzu Corporation

컬럼 : Xterra RP18, 250mm x 4.6mm, 5㎛Column: Xterra RP18, 250 mm x 4.6 mm, 5 μm

용출제 : 아세토니트닐 / 인산 완충액(pH 3) = 6 : 4Eluent: acetonitrile / phosphate buffer (pH 3) = 6: 4

유속 : 1.5㎖ / 분Flow rate: 1.5ml / min

투입량 : 10㎕Input amount: 10µl

검출 : 238nm(UV 검출기)Detection: 238 nm (UV detector)

온도 : 40℃Temperature: 40 ℃

비교예 1. 구조식 (I)의 디올락톤의 제조방법(미국 특허 제 4,444,784호 기재제법)Comparative Example 1. Method for preparing diolactone of structural formula (I) (based on US Pat. No. 4,444,784)

로바스타틴 8.0g과 수산화리튬 일수화물 8.31g을 정제수 600㎖에 용해하여 질소하에서 56시간 동안 환류 교반하였다. 반응물을 0℃ 로 냉각하여 20㎖ 염산으로 중화한 후에, 에테르 200㎖로 각각 4회 추출하고, 포화 소금물로 세척 후, 망초를 사용하여 건조, 여과 및 농축하였다. 농축물에 200㎖의 톨루엔을 가하여 2시간 동안 환류시킨 후, 감압, 농축하고 헥산을 가하여 결정화시켜 흰색 결정 5.15g(수율 : 81%)을 수득하였다.8.0 g of lovastatin and 8.31 g of lithium hydroxide monohydrate were dissolved in 600 ml of purified water, and the mixture was stirred under reflux for 56 hours under nitrogen. The reaction was cooled to 0 ° C. and neutralized with 20 mL hydrochloric acid, then extracted four times with 200 mL ether, washed with saturated brine, then dried, filtered and concentrated using forget-me-not. 200 ml of toluene was added to the concentrate, and the mixture was refluxed for 2 hours, concentrated under reduced pressure, and crystallized by addition of hexane to give 5.15 g (yield: 81%) of white crystals.

비교예 2. 구조식 (I)의 디올락톤의 제조방법(한국 특허 공개 제 10-2001-0040760호 기재제법)Comparative Example 2. Method for Producing Diolactone of Structural Formula (I) (Korean Patent Publication No. 10-2001-0040760

t-부탄올 300㎖중 KOH 7.92g의 용액에 로바스타틴 8.09g을 첨가하고 혼합물을 아르곤 기체하에서 30분간 교반했다. 그 후, 온도를 상승시키고 혼합물을 4시간동안 교반하면서 환류시켰다. 상기 반응 혼합물을 감압 농축시키고, 물을 첨가하고, 인산(pH 3.5)으로 산성화시키고, 에틸 아세테이트로 추출했다. 추출물을 감압 농축시켜서 갈색 오일을 수득했다. 상기 갈색 오일을 이소프로필 아세테이트 200㎖에 용해시키고, 메탄술폰산 65㎕를 첨가한 후, 용액을 감압하에 약 1/5 부피로 농축시켰다. 얻어진 잔류물을 탄산수소나트륨 포화 수용액으로 세척하고, -20℃로 냉각시켜 교반했다. 생성된 슬러리를 여과하고, 진공 건조시켜 백색 결정 5.76g(수율 : 90%)을 수득했다.To a solution of 7.92 g of KOH in 300 mL of t-butanol was added 8.09 g of lovastatin and the mixture was stirred for 30 minutes under argon gas. The temperature was then raised and the mixture was refluxed with stirring for 4 hours. The reaction mixture was concentrated under reduced pressure, water was added, acidified with phosphoric acid (pH 3.5) and extracted with ethyl acetate. The extract was concentrated under reduced pressure to give a brown oil. The brown oil was dissolved in 200 ml of isopropyl acetate, 65 μl of methanesulfonic acid was added, and then the solution was concentrated to about 1/5 volume under reduced pressure. The obtained residue was washed with saturated aqueous sodium hydrogen carbonate solution, cooled to -20 ° C and stirred. The resulting slurry was filtered and dried in vacuo to give 5.76 g (yield: 90%) of white crystals.

실시예 1. 구조식 (I)의 디올락톤의 제조방법 1Example 1 Preparation of Diolactone of Structural Formula (I) 1

테트라히드로퓨란 200g과 노말프로판올 200g을 혼합하고 로바스타틴 100g 과 수산화칼륨 100g을 가하고 반응온도를 상승시켜 2시간 환류 교반하였다. 상기 반응 혼합물을 감압하에서 농축하고 정제수 500g을 가한 후 염산 160g을 가하여 산성화하였다. 에틸 아세테이트 500g으로 추출하고 감압하에서 농축하여 얻어진 잔사에 톨루엔 600g과 인산 5g을 투입하여 1시간동안 환류 교반 하였다. 감압 농축하여 얻어진 잔사에 헥산 600g을 투입하여 결정화 하였다. 생성된 고체를 여과하고 50℃에서 건조하여 백색의 표제화합물 78g(수율 : 98.5%; HPLC 순도 : 99.2%)을 수득하였다.200 g of tetrahydrofuran and 200 g of normal propanol were mixed, 100 g of lovastatin and 100 g of potassium hydroxide were added, and the reaction temperature was raised to reflux and stirred for 2 hours. The reaction mixture was concentrated under reduced pressure, 500 g of purified water was added thereto, followed by acidification with 160 g of hydrochloric acid. Toluene 600g and phosphoric acid 5g were added to the residue obtained by extraction with 500 g of ethyl acetate and concentrated under reduced pressure, followed by stirring under reflux for 1 hour. 600 g of hexane was added to the residue obtained by concentration under reduced pressure, and crystallization was performed. The resulting solid was filtered and dried at 50 ° C. to give 78 g of a white title compound (yield: 98.5%; HPLC purity: 99.2%).

실시예 2. 구조식 (I)의 디올락톤의 제조방법 2Example 2 Preparation of Diolactone of Structural Formula (I) 2

테트라히드로퓨란 200g 과 이소프로판올 200g을 사용한 점을 제외하고는 실시예 1와 동일한 제조공정을 거쳐 백색의 표제화합물 79g(수율 : 99.7%; HPLC 순도 : 98.7%)을 수득하였다.Except for using 200 g of tetrahydrofuran and 200 g of isopropanol, 79 g of a white title compound (yield: 99.7%; HPLC purity: 98.7%) were obtained in the same manner as in Example 1.

실시예 3. 구조식 (I)의 디올락톤의 제조방법 3Example 3 Preparation of Diolactone of Structural Formula (I) 3

테트라히드로퓨란 200g 과 노말부탄올 200g을 사용한 점을 제외하고는 실시예 1와 동일한 제조공정을 거쳐 백색의 표제화합물 77g(수율 : 97.2%; HPLC 순도 : 98.5%)을 수득하였다.Except for using 200 g of tetrahydrofuran and 200 g of normal butanol, 77 g of a white title compound (yield: 97.2%; HPLC purity: 98.5%) was obtained in the same manner as in Example 1.

실시예 4. 구조식 (I)의 디올락톤의 제조방법 4Example 4 Preparation of Diolactone of Structural Formula (I) 4

테트라히드로퓨란 200g, 노말부탄올 100g 및 이소프로판올 100kg을 사용한 점을 제외하고는 실시예 1와 동일한 제조공정을 거쳐 백색의 표제화합물 77g(수율 : 97.2%; HPLC 순도 : 98.0%)을 수득하였다.Except that 200 g of tetrahydrofuran, 100 g of normal butanol and 100 kg of isopropanol were used, the same procedure as in Example 1 was carried out, and 77 g of a white title compound (yield: 97.2%; HPLC purity: 98.0%) was obtained.

실험예 1. 순도 및 수율확인 실험Experimental Example 1. Purity and yield confirmation experiment

실시예 1의 방법과 비교예 1 및 2의 방법을 상호비교하여 반응시간 및 단계별 생성물의 양을 각각 측정하여 하기 표 1에 나타내었다.The method of Example 1 and the methods of Comparative Examples 1 and 2 were compared with each other to measure the reaction time and the amount of step products, respectively, and are shown in Table 1 below.

비교예 1Comparative Example 1 비교예 2Comparative Example 2 실시예 1Example 1 반응시간Reaction time 2시간2 hours 56시간56 hours 2시간2 hours 4시간4 hours 2시간2 hours 트리올산Trioleic acid 2.3%2.3% 85.5%85.5% 81.2%81.2% 89.5%89.5% 97.4%97.4% 디올 락톤Dior lactone 0.0%0.0% 2.4%2.4% 0.5%0.5% 2.5%2.5% 2.0%2.0% 미확인불순물Unidentified Impurities 0.550.55 11.6%11.6% 3.3%3.3% 7.8%7.8% 0.6%0.6% 로바스타틴Lovastatin 97.2%97.2% 0.5%0.5% 15%15% 0.2%0.2% 0.0%0.0% 최종 디올 락톤의 분리 수율 및 순도Separation Yield and Purity of Final Diol Lactone 81%81% 90%(95.1%)90% (95.1%) 98.5%98.5%

상기 표 1에서 알 수 있는 바와 같이, 본원 발명에 의한 제조방법은 비교예1 및 2에 비하여 수율면에서 최종 디올 락톤의 분리수율(98.5∼99.7%)이 현저히 높으며, 제 1단계를 통한 트리올산의 제조시 트리올산 및 디올 락톤 생성물의 순도(98.5∼99.7%, 반응 중 HPLC로 측정)도 또한 종래의 방법에 의한 순도에 비해 월등히 향상되었음을 알 수 있었다.As can be seen in Table 1, the production method according to the present invention has a significantly higher separation yield (98.5-99.7%) of the final diol lactone in terms of yield compared to Comparative Examples 1 and 2, triol acid through the first step It was also found that the purity (98.5-99.7%, measured by HPLC in the reaction) of the triol acid and diol lactone products in the preparation of was also significantly improved compared to the purity by conventional methods.

본 발명의 제조방법은 혼합용매를 사용함으로써 강염기하에서도 보다 더 안정적으로 가수분해를 수행함으로써, 구조식(II)의 트리올산을 고순도 및 고수율로 제조하고 이를 락톤화 함으로써 심바스타틴의 중간체인 구조식(I)의 디올 락톤을 경제적이고 공업적으로 유용하게 합성할 수 있는 보다 향상된 제조방법을 제공할 수 있다.In the production method of the present invention, hydrolysis is performed more stably under a strong base by using a mixed solvent, thereby preparing triol acid of formula (II) in high purity and high yield and lactonizing the structural formula (I), which is an intermediate of simvastatin. It is possible to provide an improved manufacturing method that can economically and industrially usefully synthesize diol lactone of a).

Claims (8)

하기 구조식(III)의 로바스타틴을 무기염기 존재하에 테트라히드로퓨란 및 1차, 2차 또는 3차 알콜용매로부터 선택된 알콜 혼합용매 중에서 반응시켜 가수분해함으로써 하기 구조식(II)의 트리올산을 제조하는 제 1단계; 상기 트리올산을 산성화 및 락톤화시켜 하기 구조식(I)의 6(R)-[2-(8'(S)-히드록시-2'(S),6'(R)-디메틸-1',2',6',7',8',8'a(R)-헥사히드로나프틸-1'(S))-에틸]-4(R)-히드록시-3,4,5,6-테트라히드로-2H-피란-2-온 디올락톤체를 제조하는 제 2단계 공정을 포함하는 심바스타틴 중간체의 제조방법.A lovastatin of formula (III) is reacted with tetrahydrofuran and an alcohol mixed solvent selected from primary, secondary or tertiary alcohol solvents in the presence of an inorganic base to prepare a triol acid of formula (II) step; The triol acid was acidified and lactoneized to give 6 (R)-[2- (8 '(S) -hydroxy-2' (S), 6 '(R) -dimethyl-1', 2 ', 6', 7 ', 8', 8'a (R) -hexahydronaphthyl-1 '(S))-ethyl] -4 (R) -hydroxy-3,4,5,6- A method for producing a simvastatin intermediate comprising a second step process of preparing a tetrahydro-2H-pyran-2-one diolactone body. 제 1항에 있어서, 제 1단계의 1차 알콜용매가 노말프로판올 또는 노말부탄올인 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the primary alcohol solvent of the first step is normal propanol or normal butanol. 제 1항에 있어서, 제 1단계의 2차 알콜용매가 이소프로판올 또는 이소부탄올인 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the secondary alcohol solvent of the first step is isopropanol or isobutanol. 제 1항에 있어서, 제 1단계의 3차 알콜용매가 t-부탄올인 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the tertiary alcohol solvent of the first step is t-butanol. 제 1항에 있어서, 제 1단계의 테트라히드로퓨란 및 혼합용매의 사용비가 1:0.5∼1.5인 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the use ratio of tetrahydrofuran and the mixed solvent in the first step is 1: 0.5 to 1.5. 제 5항에 있어서, 제 1단계의 테트라히드로퓨란 및 혼합용매의 사용비가 1 : 1 인 것을 특징으로 하는 제조방법.The method according to claim 5, wherein the use ratio of tetrahydrofuran and the mixed solvent of the first step is 1: 1. 제 1항에 있어서, 제 1단계의 무기염기가 수산화리튬, 수산화나트륨 또는 수산화칼륨인 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the inorganic base of the first step is lithium hydroxide, sodium hydroxide or potassium hydroxide. 제 1항에 있어서, 제 1단계의 반응시간이 1시간 내지 3시간인 것을 특징으로 하는 제조방법.The method of claim 1, wherein the reaction time of the first step is 1 hour to 3 hours.
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