KR20020071637A - A purification method of pravastatin using methanol - Google Patents
A purification method of pravastatin using methanol Download PDFInfo
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- KR20020071637A KR20020071637A KR1020010011793A KR20010011793A KR20020071637A KR 20020071637 A KR20020071637 A KR 20020071637A KR 1020010011793 A KR1020010011793 A KR 1020010011793A KR 20010011793 A KR20010011793 A KR 20010011793A KR 20020071637 A KR20020071637 A KR 20020071637A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/48—Separation; Purification; Stabilisation; Use of additives
- C07C67/56—Separation; Purification; Stabilisation; Use of additives by solid-liquid treatment; by chemisorption
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
- B01D15/26—Selective adsorption, e.g. chromatography characterised by the separation mechanism
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
- B01J31/08—Ion-exchange resins
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/76—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring
- C07C69/94—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring of polycyclic hydroxy carboxylic acids, the hydroxy groups and the carboxyl groups of which are bound to carbon atoms of six-membered aromatic rings
Abstract
Description
본 발명은 프라바스타틴의 정제방법에 관한 것으로서, 더욱 상세하게는 HP20수지 또는 HP20ss와 메탄올을 이용하여 흡착 크로마토그래피를 함으로써 프라바스타틴을 정제하는 것이다.The present invention relates to a method for purifying pravastatin, and more particularly, purastatin is purified by adsorption chromatography using HP20 resin or HP20ss and methanol.
프라바스타틴 전구체 콤펙틴은 콜레스테롤 농도를 저하시킬 수 있는 물질로서 미합중국 특허공고 제 3,983,140호 및 영국특허 제 1,453,425호에 개시되어 있다. 이는 콜레스테롤 농도를 저하시킴으로써 과지방혈증, 특히 고지혈증으로 인한 심근경색증 또는 동맥경화증과 같은 심장병에 효과가 있는 물질이다.Pravastatin precursor compactin is disclosed in US Pat. Nos. 3,983,140 and 1,453,425 as substances capable of lowering cholesterol concentrations. It is a substance that is effective in heart disease such as myocardial infarction or arteriosclerosis caused by hyperlipidemia, especially hyperlipidemia by lowering cholesterol concentration.
이러한 프라바스타틴 전구체의 제조방벙에 사용되는 균주로는 페니실리움 브레비콤팩틴(Penicillium brevicompactin), 페니실마이세스속(Penicilmyces sp.), 트리코데르마 론기브라이아튬(Tricoderma longibraiatum), 트리코데르마 슈도코닌기이(Tricoderma psudokoning), 하이포마이세스 크리소포러스(Hyphomyces chrisopomus) 및 페니실리움 시트리눔(Phenicillium citrinum)을 들 수 있다[일본국 특허 공고 제 (평)4-349034호]. 이러한 균주 또는 화학적 변환작용에 의해 프라바스타틴 전구체가 제조될 수 있다. 또한 대한민국 특허 제 0186758호에는 글리오클라디움속(Gliocladium sp.) YJ-9515 (KCTC 02528BP)를 호기적으로 배양하여 프라바스타틴 전구체 콤펙틴 및 그의 유도체를 제조하는 방법이 개시되어 있다.Strains used in the preparation of such pravastatin precursors include Penicillium brevicompactin, Penicillmyces sp., Trichoderma longibraiatum, Tricorderma pseudo Trichoderma psudokoning, Hyphomyces chrisopomus, and Penicillium citrinum (Japanese Patent Publication No. 4-349034). Pravastatin precursors can be prepared by such strains or chemical transformations. In addition, Korean Patent No. 0186758 discloses a method of preparing pravastatin precursor compactin and its derivatives by aerobic culturing of Gliocladium sp. YJ-9515 (KCTC 02528BP).
대한민국 특허 제 100212482호에는 스트렙토마이세스 엑스포리아투스 (Streptomyces exfoliatus) YJ-118를 이용하여 프라바스타틴 나트륨을 제조하는 방법이 개시되어 있고, 제 0186706호에는 스트렙토마이세스 로세오크로모게네스 아종(Streptomyces roseochromogenes subsp.)인 KTCC 12385의 배양액에 프라바스타틴 전구체를 첨가·배양하여 프라바스타틴 나트륨을 제조하는 방법이 기술되어 있다.Korean Patent No. 100212482 discloses a method for preparing pravastatin sodium using Streptomyces exfoliatus YJ-118, and No. 0186706 to Streptomyces roseochromogenes subsp. A method of preparing pravastatin sodium by adding and culturing pravastatin precursor to a culture medium of KTCC 12385 is described.
프라바스타틴은 프라바스타틴 전구체 콤펙틴 및 그의 유도체에 미생물을 발효하여 전환시켜 생산한다. 이때 발효가 끈난 발효액 중에는 프라바스타틴 전구체 콤펙틴 및 그의 유도체가 남아 있어 정제에 어려움이 있다.Pravastatin is produced by fermenting and converting microorganisms to pravastatin precursor compactin and its derivatives. At this time, in the fermentation broth sticking to fermentation, pravastatin precursor compactin and its derivatives remain, which makes it difficult to purify.
본 발명은 프라바스타틴 전구체로부터 생성된 프라바스타틴을 메탄올 및 HP20 또는 HP20ss을 이용한 컬럼 크로마토그래피하고, 흡착시와 용리시의 메탄올 농도를 조절함으로써 프라바스타틴만을 고수율로 정제하는 방법을 제공하는 것이다. 일반적으로 프라바스타틴은 전구체를 균주와 함께 발효시켜 생성되는데 이는 정제과정에 어려움이 있다. 본 발명의 방법에 따라 이러한 프라바스타틴 전구체와 프라바스타틴을 효율적으로 분리할 수 있다.The present invention provides a method for purifying only pravastatin by column chromatography of pravastatin produced from pravastatin precursor using methanol and HP20 or HP20ss, and adjusting the methanol concentration at the time of adsorption and elution. In general, pravastatin is produced by fermenting a precursor with a strain, which is difficult to purify. According to the method of the present invention, such pravastatin precursor and pravastatin can be efficiently separated.
본 발명은 프라바스타틴을 정제하기 위한 방법으로 HP20수지 또는 HP20ss를 사용한 흡착 크로마토그래피를 이용할 경우,The present invention uses the adsorption chromatography using HP20 resin or HP20ss as a method for purifying pravastatin,
흡착시 흡착용액 중의 메탄올의 농도를 10%이하로 하여 흡착시키고At the time of adsorption, the concentration of methanol in the adsorption solution
용리시 용리용액 중의 메탄올 농도를 20%이상로 하여 용리시키는 것을 특징으로 하여 불순물을 제거함으로써 프라바스타틴을 정제하는 방법에 관한 것이다.The present invention relates to a method for purifying pravastatin by removing impurities by eluting at a concentration of 20% or more of the methanol in the eluting solution during elution.
본 발명에서 프라바스타틴 전구체의 생산균주로서 스트렙토마이세스속(Streptomyces sp.)를 사용하여 제조한다.In the present invention, the production strain of pravastatin precursor is prepared using Streptomyces sp.
즉, 프라바스타틴 전구체 콤펙틴 및 그의 유도체를 포함하는 배양액을 스트렙토마이세스속 균주에 첨가하여 이를 함께 공배양 발효함으로써 전구체 콤펙틴 등으로부터 프라바스타틴을 제조한다. 이 후, HP20 수지 및 HP20ss를 팩킹시킨 컬럼 크로마토그래피에서 전개시켜 이 발효물 중의 프라바스타틴을 수지에 흡착시킨다. 이 경우 흡착용액으로 메탄올을 20%이하 농도로 포함하는 용액을 사용한다. 흡착된 프라바스타틴을 메탄올을 20% 이상 농도로 함유하는 용리용액으로 용리시킴으로써 프라바스타틴을 수득한다.That is, pravastatin is prepared from the precursor compactin by adding a culture solution containing the pravastatin precursor compactin and derivatives thereof to a strain of the genus Streptomyces and co-culturing the same together. Thereafter, HP20 resin and HP20ss are developed in packed column chromatography to adsorb pravastatin in this fermentation product to the resin. In this case, a solution containing methanol at a concentration of 20% or less is used as the adsorption solution. Pravastatin is obtained by eluting the adsorbed pravastatin with an eluent containing at least 20% methanol.
흡착액은 사용한 발효여액 및 혼합액으로 흡착액 중에 프라바스타틴 1 g/l, ML236B 및 그의 유도체 0.2 g/l를 사용하였다.As the fermentation filtrate and the mixed solution used, 1 g / l of pravastatin, 0.2 g / l of ML236B and its derivatives were used in the adsorption liquid.
실시예 1 흡착액을 HP20 수지에 흡착시 메탄올(IPA)의 영향Example 1 Effect of Methanol (IPA) on Adsorption of Adsorbents on HP20 Resin
HP20수지용량: 200ml, 흡착액량: 1000ml(프라바스타틴 1000mg/l, 콤펙틴과 그의 유도체 200mg/l), 색도는 OD660nm를 측정하였고, 흡착원액의 색도를 100으로 하여 환산하였다.HP20 resin capacity: 200ml, adsorption liquid volume: 1000ml (pravastatin 1000mg / l, Compectin and its derivatives 200mg / l), the chromaticity was measured by OD660nm, the color of the adsorption stock solution was converted to 100.
결과:result:
흡착액중에 알코올 함량을 10%이하로 흡착한 흡착여액 중에는 프라바스타틴만을 함유하고 있었고, 수율은 56 -72%이었다. 알코올이 20%함유한 흡착액의 통과액중에는 프라바스타틴 수율은 80%이었다. 알코올이 30%이상을 함유한 흡착액의 통과액중에는 프라바스타틴과 콤펙틴과 그의 유도체가 흡착한 원과 비슷한 구성비로 함유되어 있었다.The adsorption filtrate which adsorbed the alcohol content below 10% contained only pravastatin and the yield was 56-72%. The pravastatin yield was 80% in the passage of the adsorbent containing 20% alcohol. The adsorbent containing 30% or more of alcohol contained the same ratio as that of the original adsorbed by pravastatin, compactin and its derivatives.
이 결과로부터 흡착액 중의 알코올 농도를 20%이하에서 흡착시켜 불순물을 제거하면서 정제수율을 향상 시킬수 있음을 알 수 있었다.From this result, it can be seen that it is possible to improve the purification yield while removing impurities by adsorbing the alcohol concentration in the adsorption liquid at 20% or less.
실시예 2 흡착수지를 용리시킬 때 용리액중의 메탄올 농도의 영향Example 2 Influence of Methanol Concentration in Eluent When Elution Resin
알코올이 없는 흡착액 1000ml을 HP20수지 200ml에 충진하여 흡착을 시킨 다음 각 용리액중에 메탄올 농도를 다르게 조제한 용리액 1000 ml를 각 수지에 통과시켜 용리시켰다.1000 ml of alcohol-free adsorbent was filled in 200 ml of HP20 resin and adsorbed, and eluted by passing 1000 ml of eluent with different methanol concentration in each eluent.
용리액중에 메탄올 함량이 10%이하일 경우는 프라바스타틴만이 용리되었고, 20%에서는 프라바스타틴 405 mg과 콤펙틴과 그의 유도체 함량이 불과 40mg이 용리되었으나, 30 %이상에서는 프라바스타틴 410mg 이상이었고, 동시에 콤펙틴과 그의 유도체 함량이 많아졌다.In case of methanol content of eluent less than 10%, only pravastatin eluted. In 20%, only pravastatin 405 mg and compactin and its derivatives were eluted; Derivative content increased.
그러므로 용리액중에 메탄올 농도를 20%이하로 하여 용리시켜 불순물을 제거하면서 정제 수율을 향상시킬 수 있다.Therefore, it is possible to improve the purification yield while removing impurities by eluting with a methanol concentration of 20% or less in the eluent.
본 발명의 정제방법을 사용하여 프라바스타틴을 정제하는 경우 추가의 공정없이 단순히 프라바스타틴 및 기타 불순물을 포함하는 발효액을 HP20 수지를 팩킹시킨 컬럼에 통과시키고 그 흡착용액과 용리용액의 메탄올 농도만을 조절함으로써 프라바스타틴을 고수율로 얻을 수 있다.When purvastatin is purified using the purification method of the present invention, pravastatin is purified by simply passing a fermentation broth containing pravastatin and other impurities through a column packed with HP20 resin, and adjusting only the methanol concentration of the adsorption solution and the elution solution without further processing. It can be obtained in high yield.
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