KR101393010B1 - A process for preparing 2-(4-formylphenyl)propionic acid by using TEMPO catalyst - Google Patents
A process for preparing 2-(4-formylphenyl)propionic acid by using TEMPO catalyst Download PDFInfo
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Abstract
본 발명은 TEMPO 촉매제를 이용한 2-(4-포르밀페닐)프로피온 산의 제조방법에 관한 것으로서, 좀더 상세히 설명하면 에스테르 용매 하에서 TEMPO(2,2,6,6-tetra methyl piperidinyl oxy free radical) 촉매제를 사용하여 출발물질인 2-[4-(하이드록시메틸)페닐]프로피온 산을 차아염소산나트륨(NaOCl) 수용액으로 산화반응 시킴으로서, 유독성 결정화 용매를 사용하지 않는 친환경적인 분위기에서 고순도의 2-(4-포르밀페닐)프로피온 산을 고수율로 제조하는 방법에 관한 것이다.The present invention relates to a process for preparing 2- (4-formylphenyl) propionic acid using a TEMPO catalyst, and more particularly, to a process for preparing 2- (4-formylphenyl) (4- (hydroxymethyl) phenyl] propionic acid, which is a starting material, is oxidized with an aqueous solution of sodium hypochlorite (NaOCl) to produce a high purity 2- - < / RTI > formylphenyl) propionic acid in high yield.
Description
본 발명은 TEMPO 촉매제를 이용한 2-(4-포르밀페닐)프로피온 산의 제조방법에 관한 것으로서, 좀더 상세히 설명하면 에스테르 용매 하에서 TEMPO(2,2,6,6-tetra methyl piperidinyl oxy free radical) 촉매제를 사용하여 출발물질인 2-[4-(하이드록시메틸)페닐]프로피온 산을 차아염소산나트륨(NaOCl) 수용액으로 산화반응 시킴으로서, 유독성 결정화 용매를 사용하지 않는 친환경적인 분위기에서 고순도의 2-(4-포르밀페닐)프로피온 산을 고수율로 제조하는 방법에 관한 것이다.
The present invention relates to a process for preparing 2- (4-formylphenyl) propionic acid using a TEMPO catalyst, and more particularly, to a process for preparing 2- (4-formylphenyl) (4- (hydroxymethyl) phenyl] propionic acid, which is a starting material, is oxidized with an aqueous solution of sodium hypochlorite (NaOCl) to produce a high purity 2- - < / RTI > formylphenyl) propionic acid in high yield.
상기 2-(4-포르밀페닐)프로피온 산[2-(4-formylphenyl)propionic acid]은 다음 반응식 1에서 보는 바와 같이 펠루비프로펜(pelubiprofen)의 제조 중간체로 사용되는 매우 유용한 화합물이다.
The 2- (4-formylphenyl) propionic acid 2- (4-formylphenyl) propionic acid is a very useful compound used as a preparation intermediate of pelubiprofen as shown in the following reaction scheme (1).
[반응식 1][Reaction Scheme 1]
잘 알려진 바와 같이, 펠루비프로펜(pelubiprofen)은 일본 상교(Sankyo)사가 개발한 비스테로이드 계열의 진통 및 소염제(NSAID)이다. 이 물질은 골관절염, 류마티스성 관절염, 근골격성통증, 수술 후 후유증, 요통, 치통 등과 같은 다양한 종류의 질병 치료에 약리활성을 보인다. 또한 이와 유사한 비스테로이드 계열의 소염진통제인 이부프로펜(ibuprofen)에 비하여서도 매우 높은 약리활성을 가진다는 연구도 보고되고 있다(Theories and Applications of Chem. Eng., 2002, Vol. 8, No. 1).As is well known, pelubiprofen is a nonsteroidal analgesic and antiinflammatory agent (NSAID) developed by Sankyo Corporation of Japan. The substance has pharmacological activity in treating various kinds of diseases such as osteoarthritis, rheumatoid arthritis, musculoskeletal pain, post-operative aftereffects, back pain, toothache and the like. It has also been reported that ibuprofen has a very high pharmacological activity compared to similar non-steroidal anti-inflammatory analgesics (Theories and Applications of Chem. Eng., 2002, Vol. 8, No. 1).
종래에 알려진 2-(4-포르밀페닐)프로피온 산의 합성방법을 살펴보면, 일본 공개특허 평04-368353호에는 하기 반응식 2와 같이, 2-[4-(하이드록시메틸)페닐]프로피온 산{2-[4-(hydroxymethyl)phenyl]propionic acid}을 에틸아세테이트 용매 및 산 조건 하에서 차아염소산나트륨(NaOCl) 수용액으로 산화시키는 방법이 보고되어 있다.
JP-A-04-368353 discloses a method for synthesizing 2- (4-formylphenyl) propionic acid, which is known in the art, by reacting 2- [4- (hydroxymethyl) phenyl] There has been reported a method of oxidizing 2- [4- (hydroxymethyl) phenyl] propionic acid} with an aqueous solution of sodium hypochlorite (NaOCl) in an ethyl acetate solvent and an acidic condition.
[반응식 2][Reaction Scheme 2]
상기 일본 공개특허에 소개된 방법은 금속 화합물이 포함되지 않은 산화반응으로써, 반응 후에 산화제를 간편하게 분해함으로써 폐기물 처리문제를 간단히 해결할 수 있는 장점이 있다. 그러나, 반응 중에 발생하는 유연물질들로 인하여 재결정을 통한 정제과정을 거쳐야 하고, 이러한 정제과정은 전체 반응의 수율을 감소시키는 원인이 된다. The method disclosed in Japanese Laid-Open Patent Publication No. 2000-34832 has an advantage that the problem of the waste treatment can be solved simply by decomposing the oxidizing agent after the reaction as an oxidation reaction not including a metal compound. However, due to the flexible substances generated during the reaction, it is required to undergo a purification process through recrystallization, and this purification process causes a reduction in the yield of the overall reaction.
또한, 상기 정제과정에서 완전히 제거되지 않은 유연물질들은 최종 제품인 펠루비프로펜의 순도를 감소시키는 원인이 되며, 나아가 결정화 과정에서 사용되는 사염화탄소는 간독성이 강한 물질로 분류되어 있어서 대량 생산 시 작업자의 안전을 보장할 수 없다는 문제가 있다.
In addition, the pellets of the final product, pellubiprofen, which have not been completely removed during the purification process, are reduced in purity. Further, since carbon tetrachloride used in the crystallization process is classified as a substance having high hepatotoxicity, Can not be guaranteed.
따라서 본 발명이 해결하고자 하는 과제는 펠루비프로펜의 제조 중간체인 2-(4-포르밀페닐)프로피온 산을 제조함에 있어서, TEMPO(2,2,6,6-tetra methyl piperidinyl oxy free radical) 촉매제를 사용하여 친환경적인 분위기에서 저렴한 비용으로 고순도의 목적물질을 고효율로 제조할 수 있는 새로운 제조방법을 제공하는 것이다.
Accordingly, a problem to be solved by the present invention is to provide a process for preparing 2- (4-formylphenyl) propionic acid which is a production intermediate of felubipropene, wherein TEMPO (2,2,6,6-tetramethylpiperidinyloxy free radical) And to provide a new production method capable of producing a high purity target substance at a high efficiency at a low cost in an environment friendly environment using a catalyst.
본 발명에 따른 2-(4-포르밀페닐)프로피온 산의 제조방법은, (a) 2-[4-(하이드록시메틸)페닐]프로피온 산을 에스테르 용매에 용해하고, 여기에 상기 2-[4-(하이드록시메틸)페닐]프로피온 산에 대하여 0.01~0.1 당량의 TEMPO(2,2,6,6-tetra methyl piperidinyl oxy free radical) 촉매제를 첨가하는 단계와; (b) 10~40 ℃의 온도에서 차아염소산나트륨(NaOCl) 10% 수용액을 상기 2-[4-(하이드록시메틸)페닐]프로피온 산에 대하여 1~1.5 당량 적가(滴加)하고 교반하는 단계와; (c) 유기층을 분리하여 농축한 다음, 에틸아세테이트와 포화탄화수소용매의 혼합용매로 결정화하는 단계; 를 포함하는 것을 특징으로 한다.
The process for producing 2- (4-formylphenyl) propionic acid according to the present invention comprises: (a) dissolving 2- [4- (hydroxymethyl) phenyl] propionic acid in an ester solvent, 0.01 to 0.1 equivalent of TEMPO (2,2,6,6-tetramethylpiperidinyl oxy free radical) catalyst to 4- (hydroxymethyl) phenyl] propionic acid; (b) dropwise adding 1 to 1.5 equivalents of a 10% aqueous solution of sodium hypochlorite (NaOCl) to the 2- [4- (hydroxymethyl) phenyl] propionic acid at a temperature of 10 to 40 ° C and stirring Wow; (c) separating and concentrating the organic layer, and crystallizing with a mixed solvent of ethyl acetate and a saturated hydrocarbon solvent; And a control unit.
본 발명은 2-(4-포르밀페닐)프로피온 산을 제조함에 있어서, 출발물질인 2-[4-(하이드록시메틸)페닐]프로피온 산을 TEMPO(2,2,6,6-tetra methyl piperidinyl oxy free radical) 촉매제 하에서 차아염소산나트륨(NaOCl) 수용액으로 산화반응 시킴으로서, 종래 방법에 비해 목적물질의 수율은 약 15% 이상, 목적물질의 순도는 약 10% 이상 향상된 효과를 얻을 수 있다.The present invention relates to a process for the preparation of 2- (4-formylphenyl) propionic acid by reacting 2- [4- (hydroxymethyl) phenyl] propionic acid as a starting material with 2,2,6,6-tetramethylpiperidinyl oxidation reaction with an aqueous solution of sodium hypochlorite (NaOCl) under an oxygen free radical catalyst enables the yield of the target material to be improved by about 15% or more and the purity of the target material by about 10% or more, compared with the conventional method.
또한, 결정화 용매로서 유독성 사염화탄소를 사용하는 대신에 저렴한 에틸아세테이트와 포화탄화수소용매의 혼합용매를 결정화 용매로 사용함으로서 친환경적이면 경제적으로 목적물질을 제조할 수 있는 효과가 있다.
In addition, instead of using toxic carbon tetrachloride as a crystallization solvent, a mixed solvent of ethyl acetate and a saturated hydrocarbon solvent is used as a crystallization solvent, so that a desired material can be produced economically and economically.
도 1은 본 발명에 따라 제조된 2-(4-포르밀페닐)프로피온 산의 핵자기공명 스펙트럼이다.1 is a nuclear magnetic resonance spectrum of 2- (4-formylphenyl) propionic acid prepared according to the present invention.
본 발명에 따른 TEMPO 촉매제를 이용한 2-(4-포르밀페닐)프로피온 산의 제조방법은 다음 반응식 3으로 표시된다.
The process for preparing 2- (4-formylphenyl) propionic acid using the TEMPO catalyst according to the present invention is represented by the following reaction formula (3).
[반응식 3][Reaction Scheme 3]
본 발명에서는 먼저 출발물질인 2-[4-(하이드록시메틸)페닐]프로피온 산을 에스테르 용매에 용해한다. 상기 에스테르 용매로는 메틸아세테이트, 에틸아세테이트, 프로필아세테이트, 이소프로필아세테이트 중에서 선택된 어느 하나 이상을 사용할 수 있으나, 이중에서 에틸아세테이트를 사용하는 것이 가장 바람직하다. In the present invention, first, 2- [4- (hydroxymethyl) phenyl] propionic acid as a starting material is dissolved in an ester solvent. As the ester solvent, at least one selected from methyl acetate, ethyl acetate, propyl acetate and isopropyl acetate may be used, and ethyl acetate is most preferably used.
다음으로 상기 2-[4-(하이드록시메틸)페닐]프로피온 산에 대하여 0.01~0.1 당량의 TEMPO(2,2,6,6-tetra methyl piperidinyl oxy free radical) 촉매제를 첨가한다. 안정한 형태의 라디칼 화합물인 상기 TEMPO는 승화성이 있는 붉은 고체로서, 주로 알코올의 산화반응 촉매로 사용된다. 짝을 이루는 산화제에 따라 알데히드 또는 카르복실산을 생성하며, 1차 알코올의 선택적 산화반응에 활성을 갖는 특징이 있다. Then, 0.01 to 0.1 equivalent of TEMPO (2,2,6,6-tetramethylpiperidinyl oxy free radical) catalyst is added to the 2- [4- (hydroxymethyl) phenyl] propionic acid. The TEMPO, which is a stable form of radical compound, is a sublimable red solid and is mainly used as an oxidation catalyst for alcohol. The aldehyde or carboxylic acid is produced according to the paired oxidizing agent and has an activity to selectively oxidize the primary alcohol.
상기 TEMPO 촉매제의 사용량이 0.01 당량 미만이면, 반응 속도가 느려지고 이로 인해 수율이 감소한다. 반대로, 0.1 당량 이상이면, 반응속도가 빨라져 부반응물이 생성되고, 원가가 높은 TEMPO의 특성상 가격 대비 효율이 감소한다. If the amount of the TEMPO catalyst used is less than 0.01 equivalent, the reaction rate is slowed and the yield is reduced. On the other hand, if it is 0.1 equivalents or more, the reaction rate is increased and side reactants are produced, and the cost efficiency is reduced due to the nature of TEMPO having a high cost.
다음은 10 wt% 차아염소산나트륨(NaOCl) 수용액을 10~40 ℃의 온도를 유지시키며 천천히 적가(滴加)한다. 이때 상기 반응 온도가 10 ℃ 미만이면, 반응 과정에서 고체가 석출되어 교반 및 반응 진행이 어려우며, 반대로 40 ℃를 초과하면 부반응물이 생성되는 문제가 있다. Next, a 10 wt% aqueous solution of sodium hypochlorite (NaOCl) is slowly added dropwise while maintaining the temperature at 10 to 40 ° C. If the reaction temperature is less than 10 ° C, the solid is precipitated in the course of the reaction and stirring and reaction progress are difficult. On the other hand, if the reaction temperature exceeds 40 ° C, side reactants are formed.
또한, 상기 차아염소산나트륨(NaOCl) 수용액을 첨가할 때는 발열반응이 일어나므로, 상기 반응 온도를 유지하기 위해서는 천천히 적가하는 것이 바람직한데, 너무 천천히 첨가하여 반응 시간이 1 시간 이상으로 길어지게 되면 부반응물이 생성되기 쉬우므로 주의하여야 한다.When an aqueous solution of sodium hypochlorite (NaOCl) is added, an exothermic reaction occurs. In order to maintain the reaction temperature, it is preferable to slowly drop the reaction mixture. When the reaction time is increased to 1 hour or more, Is easy to generate.
마지막으로 상기 반응용액의 수층과 유기층을 분리하고, 무수황산나트륨으로 건조 및 농축한 다음, 에틸아세테이트와 포화탄화수소용매의 혼합용매로 결정화하여 본 발명의 목적물질인 2-(4-포르밀페닐)프로피온 산을 수득한다.Finally, the aqueous layer of the reaction solution and the organic layer were separated, dried over anhydrous sodium sulfate and concentrated, and then crystallized with a mixed solvent of ethyl acetate and a saturated hydrocarbon solvent to obtain 2- (4-formylphenyl) propionate Acid.
이때, 공용매(co-solvent)로 사용되는 상기 포화탄화수소용매로는 노르말펜탄, 노르말헥산, 노르말헵탄 중에서 선택된 어느 하나 이상을 사용할 수 있다. 상기 결정화 용매로는 에틸아세테이트와 노르말헵탄의 혼합용매를 사용하는 것이 바람직하다.
At this time, as the saturated hydrocarbon solvent used as a co-solvent, at least one selected from n-pentane, n-hexane, and n-heptane can be used. As the crystallization solvent, it is preferable to use a mixed solvent of ethyl acetate and n-heptane.
이하, 본 발명에 대한 실시예를 들어보면 다음과 같다.
Hereinafter, an embodiment of the present invention will be described.
[실시예 1 ~ 9][Examples 1 to 9]
250 ml의 반응용기에 15 g의 2-[4-(하이드록시메틸)페닐]프로피온 산을 넣고 다음 표 1의 에스테르 용매 150 ml를 투입하였다. 이어 TEMPO 촉매제를 0.01~0.1 당량(표 1 참조) 첨가한 뒤, 10 wt% 차아염소산나트륨(NaOCl) 수용액을 10~40 ℃의 온도에서 천천히 적가하고, 30분 동안 교반한 후, 유기층과 물층을 분리하였다. 15 g of 2- [4- (hydroxymethyl) phenyl] propionic acid was placed in a reaction vessel of 250 ml, and 150 ml of the ester solvent shown in Table 1 below was added. Then, a 10 wt% aqueous solution of sodium hypochlorite (NaOCl) was slowly added dropwise at a temperature of 10 to 40 ° C, and the mixture was stirred for 30 minutes. Then, an organic layer and a water layer Respectively.
상기 유기층을 무수황산나트륨(sodium sulfate)으로 건조, 감압 및 농축한 후 에틸아세테이트와 포화탄화수소용매의 혼합용매를 결정화 용매로 사용하여 백색의 고체상 목적물질을 수득하였다. 각 실시예 별로 확인된 목적물질의 수율 및 순도는 다음 표 1과 같다.
The organic layer was dried over anhydrous sodium sulfate, concentrated under reduced pressure, and a mixed solvent of ethyl acetate and a saturated hydrocarbon solvent was used as a crystallization solvent to obtain a white solid object compound. The yield and purity of the target material identified for each example are shown in Table 1 below.
촉매제
(당량)TEMPO
Catalyst
(equivalent weight)
용매reaction
menstruum
(당량)NaOCl
(equivalent weight)
온도reaction
Temperature
상기 표 1에서, TEMPO 촉매제와 차아염소산나트륨(NaOCl)의 당량은 출발물질인 2-[4-(하이드록시메틸)페닐]프로피온 산의 몰(mole)에 대한 상대적 값을 나타낸다.
In Table 1, the equivalent of the TEMPO catalyst and sodium hypochlorite (NaOCl) represents the relative value to the mole of the starting material 2- [4- (hydroxymethyl) phenyl] propionic acid.
[비교예][Comparative Example]
250 ml의 반응용기에 10 g의 2-[4-(하이드록시메틸)페닐]프로피온 산을 넣고, 에틸아세테이트 100 ml를 투입하였다. 이어서 1N HCl 70 ml를 첨가한 뒤 30 ℃에서 교반 하에 10 wt% 차아염소산(NaClO) 수용액 46.7 ml(1.13 당량)를 1시간 동안 첨가하였다. In a reaction vessel of 250 ml, 10 g of 2- [4- (hydroxymethyl) phenyl] propionic acid was added, and 100 ml of ethyl acetate was added. Subsequently, 70 ml of 1N HCl was added and 46.7 ml (1.13 equivalents) of a 10 wt% aqueous hypochlorous acid solution (NaClO) were added at 30 ° C with stirring for 1 hour.
같은 온도에서 10분간 정치한 후 수층을 분리하고, 유기층을 Na2SO3 수용액으로 세척한 후 용매를 제거하여 결정을 분리하였다. 이 결정을 사염화탄소 45 ml로 재결정하여 목적물질(수율 78%, 순도 86%)을 수득하였다.After standing at the same temperature for 10 minutes, the aqueous layer was separated, and the organic layer was washed with an aqueous solution of Na 2 SO 3 and the solvent was removed to separate the crystals. This crystal was recrystallized from 45 ml of carbon tetrachloride to obtain the target substance (yield 78%, purity 86%).
참고로 상기 비교예는 앞서 종래 기술로 소개한 일본 공개특허 평04-368353호에 기재된 방법으로 실시한 것이다.
For reference, the comparative example was carried out by the method described in Japanese Laid-Open Patent Publication No. 04-368353, which was previously disclosed in the prior art.
[핵자기공명 스펙트럼 분석][Nuclear Magnetic Resonance Spectrum Analysis]
상기 실시예 1에서 목적물질로 수득된 2-(4-포르밀페닐)프로피온 산 화합물에 대해 핵자기공명(NMR) 데이터를 분석한 결과, 도 1에서 보는 바와 같이 d 12.50(s, 1H), 9.99(s, 1H), 7.58(d, 2H), 7.53(d, 2H), 3.83(m, 1H), 1.40(d, 3H)에서 각각 피크를 보였다. 이때, 핵자기공명(NMR)의 측정조건은 다음과 같다.NMR analysis of the 2- (4-formylphenyl) propionic acid compound obtained as the target material in Example 1 revealed that d 12.50 (s, 1H), 1H), 7.58 (d, 2H), 7.53 (d, 2H), 3.83 (m, 1H) and 1.40 (d, 3H). At this time, measurement conditions of nuclear magnetic resonance (NMR) are as follows.
1) 장치 : Bruker Model DRX NMR 4001) Apparatus: Bruker Model DRX NMR 400
2) 측정 범위: -1.0 ~ 15 ppm2) Measuring range: -1.0 ~ 15 ppm
3) 스캔 횟수: 16
3) Number of scans: 16
상기 도 1의 핵자기공명 스펙트럼 데이터로부터 본 발명에 따라 제조된 목적물질이 순수한 2-(4-포르밀페닐)프로피온 산임을 확인할 수 있다. 또한, 상기 실시예 및 비교예의 결과로부터 본 발명에 따른 2-(4-포르밀페닐)프로피온 산의 제조방법은 종래 방법에 비해 목적물질의 수율은 약 15% 이상, 목적물질의 순도는 약 10% 이상 향상된 효과를 나타낸다는 것을 알 수 있다. 또한, 결정화 용매로서 맹독성의 사염화탄소를 사용하지 않기 때문에 작업 환경이 매우 친환경적인 분위기로 개선된 효과도 얻을 수 있다.From the nuclear magnetic resonance spectrum data of FIG. 1, it can be confirmed that the target substance prepared according to the present invention is pure 2- (4-formylphenyl) propionate. Further, from the results of the above Examples and Comparative Examples, it can be seen that the yield of the target substance is about 15% or more and the purity of the target substance is about 10 % ≪ / RTI > In addition, since no carbon tetrachloride is used as a crystallization solvent, the working environment can be improved to a highly environmentally friendly atmosphere.
Claims (4)
(b) 10~40 ℃의 온도에서 차아염소산나트륨(NaOCl) 10% 수용액을 상기 2-[4-(하이드록시메틸)페닐]프로피온 산에 대하여 1~1.5 당량 적가(滴加)하고 교반하는 단계와;
(c) 유기층을 분리하여 농축한 다음, 에틸아세테이트와 포화탄화수소용매의 혼합용매로 결정화하는 단계;
를 포함하는 것을 특징으로 하는 TEMPO 촉매제를 이용한 2-(4-포르밀페닐)프로피온 산의 제조방법.
(a) 2- [4- (hydroxymethyl) phenyl] propionic acid is dissolved in an ester solvent and thereto is added 0.01 to 0.1 equivalent of TEMPO ( 2,2,6,6-tetra methyl piperidinyl oxy free radical) catalyst;
(b) dropwise adding 1 to 1.5 equivalents of a 10% aqueous solution of sodium hypochlorite (NaOCl) to the 2- [4- (hydroxymethyl) phenyl] propionic acid at a temperature of 10 to 40 ° C and stirring Wow;
(c) separating and concentrating the organic layer, and crystallizing with a mixed solvent of ethyl acetate and a saturated hydrocarbon solvent;
(4-formylphenyl) propionic acid using a TEMPO catalyst.
The process according to claim 1, wherein the ester solvent used in step (a) is at least one selected from the group consisting of methyl acetate, ethyl acetate, propyl acetate and isopropyl acetate. Methylphenyl) propionic acid.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04368353A (en) * | 1991-06-13 | 1992-12-21 | Sankyo Co Ltd | Production of 2-(p-formylphenyl)propionic acid |
JPH0952862A (en) * | 1995-08-10 | 1997-02-25 | Kuraray Co Ltd | Production of 2-or 3-(substituted) phenylpropionic acid |
US20060004200A1 (en) | 2004-06-21 | 2006-01-05 | Srinivasulu Gudipati | Processes to produce intermediates for rosuvastatin |
KR101162648B1 (en) | 2003-01-30 | 2012-07-05 | 뉴트라스위트 프라퍼티 홀딩스 인코포레이티드 | Bromine free tempo based catalyst system for oxidation of primary and secondary alcohols using naocl as an oxidant |
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH04368353A (en) * | 1991-06-13 | 1992-12-21 | Sankyo Co Ltd | Production of 2-(p-formylphenyl)propionic acid |
JPH0952862A (en) * | 1995-08-10 | 1997-02-25 | Kuraray Co Ltd | Production of 2-or 3-(substituted) phenylpropionic acid |
KR101162648B1 (en) | 2003-01-30 | 2012-07-05 | 뉴트라스위트 프라퍼티 홀딩스 인코포레이티드 | Bromine free tempo based catalyst system for oxidation of primary and secondary alcohols using naocl as an oxidant |
US20060004200A1 (en) | 2004-06-21 | 2006-01-05 | Srinivasulu Gudipati | Processes to produce intermediates for rosuvastatin |
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