KR20210073972A - A new process for the preparation of (R)-2-((4-Aminophenethyl)amino)-1-phenylethanol - Google Patents

A new process for the preparation of (R)-2-((4-Aminophenethyl)amino)-1-phenylethanol Download PDF

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KR20210073972A
KR20210073972A KR1020190164830A KR20190164830A KR20210073972A KR 20210073972 A KR20210073972 A KR 20210073972A KR 1020190164830 A KR1020190164830 A KR 1020190164830A KR 20190164830 A KR20190164830 A KR 20190164830A KR 20210073972 A KR20210073972 A KR 20210073972A
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phosphate
phenylethanol
amino
aminophenethyl
ammonium
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KR102350458B1 (en
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류형선
안진우
김지연
노경탁
엄운용
이규혁
이주철
신동균
김도경
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주식회사 다산제약
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/08Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reactions not involving the formation of amino groups, hydroxy groups or etherified or esterified hydroxy groups
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C209/00Preparation of compounds containing amino groups bound to a carbon skeleton
    • C07C209/30Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds
    • C07C209/32Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups
    • C07C209/36Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups by reduction of nitro groups bound to carbon atoms of six-membered aromatic rings in presence of hydrogen-containing gases and a catalyst
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C209/00Preparation of compounds containing amino groups bound to a carbon skeleton
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
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    • C07C215/00Compounds containing amino and hydroxy groups bound to the same carbon skeleton
    • C07C215/02Compounds containing amino and hydroxy groups bound to the same carbon skeleton having hydroxy groups and amino groups bound to acyclic carbon atoms of the same carbon skeleton
    • C07C215/22Compounds containing amino and hydroxy groups bound to the same carbon skeleton having hydroxy groups and amino groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being unsaturated
    • C07C215/28Compounds containing amino and hydroxy groups bound to the same carbon skeleton having hydroxy groups and amino groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being unsaturated and containing six-membered aromatic rings
    • C07C215/30Compounds containing amino and hydroxy groups bound to the same carbon skeleton having hydroxy groups and amino groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being unsaturated and containing six-membered aromatic rings containing hydroxy groups and carbon atoms of six-membered aromatic rings bound to the same carbon atom of the carbon skeleton
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Abstract

The present invention relates to a method for preparing (R)-2-((4-aminophenethyl)amino)-1-phenylethanol, a mirabegron intermediate, in which it is possible to prepare an amide derivative of high purity and high yield without formation of side reactants by using a zinc powder reduction catalyst, and by using the same, it is possible to prepare the mirabegron with high-purity and high-yield without a special purification process.

Description

(R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 신규한 제조방법{A new process for the preparation of (R)-2-((4-Aminophenethyl)amino)-1-phenylethanol}(R)-2-((4-Aminophenethyl)amino)-1-phenylethanol A new process for the preparation of (R)-2-((4-Aminophenethyl)amino)-1 -phenylethanol}

본 발명은 미라베그론 중간체인 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 신규한 제조방법에 관한 것이다.The present invention relates to a novel method for preparing (R)-2-((4-aminophenethyl)amino)-1-phenylethanol, which is an intermediate of mirabegron.

국제특허공보 WO13/119910에 의하면 과민성 방광 질환은 빈뇨 및 야간뇨를 동반하는 급뇨의 복합적 증상으로 정의되며, 이와 같은 증상은 대개 방광의 불수의적 수축과 연관되어 있다. 방광에는 퓨린 수용체와 교감신경이 작용하는 베타 3 수용체가 존재하며, 베타 3 수용체는 노르에피네프린과 결합하여 사이클릭 아데노신 모노 포스페이트(cAMP)의 농도를 증가시켜 방광 평활근을 이완시키고, 방광 용적을 확장하여 배뇨 간격을 연장시키는 효과를 갖는다. 미라베그론(Mirabegron)은 강력하고 선택적인 베타 3 수용체 작용물질로서, 래트 및 인간의 방광 조직에서 cAMP 농도 증가 및 방광 평활근의 이완을 보였으며, 이는 미라베그론이 방광의 베타 3 수용체를 자극하여 소변 저장기능을 증진시키는 것을 나타낸다. 일본아스텔라스제약에서 개발된 미라베그론은 베타 3 수용체 작용제로 작용하는 과민성 방광 치료제로서 2012년 6월 28일 FDA 승인을 받았으며, 국내에서는 2013년 한국아스텔라스제약이 식약처 승인을 받아 베타미가(Betmiga)로 판매되고 있다.According to International Patent Publication WO13/119910, overactive bladder disease is defined as a complex symptom of urgency accompanied by frequent urination and nocturia, and this symptom is usually associated with involuntary contraction of the bladder. In the bladder, there are beta 3 receptors, which act as purine receptors and sympathetic nerves, and beta 3 receptors bind norepinephrine and increase the concentration of cyclic adenosine monophosphate (cAMP) to relax the bladder smooth muscle and expand the bladder volume. It has the effect of extending the interval between urination. Mirabegron is a potent and selective beta 3 receptor agonist, which showed an increase in cAMP concentration and relaxation of bladder smooth muscle in rat and human bladder tissues, indicating that mirabegron stimulates bladder beta 3 receptors. It is shown to enhance urine storage function. Mirabegron, developed by Astellas Pharmaceuticals of Japan, was approved by the FDA on June 28, 2012 as a treatment for overactive bladder acting as a beta 3 receptor agonist. It is sold as Betmiga.

과민성 방광(overactive bladder, OAB) 환자에게서 발생할 수 있는 빈뇨, 야간뇨, 절박성 요실금 증상의 치료에는 현재 프로피베린 염산염 및 옥시부티닌 염산염 등의 항콜린제가 주로 사용되고 있으나, 약물에 대한 내성과 배출 장애, 목마름 증상, 가려움증, 변비, 홍반 등 항콜린제에 존재하는 부작용이 야기되어, 이를 극복하기 위해 베타 3 수용체 자극 작용을 기전으로 하는 약물인 미라베그론이 사용되고 있다. 미라베그론은 항콜린제와 달리 부교감신경 작용에 영향을 주지 않기 때문에 배뇨 단계에서 급성 요정체의 발생 위험을 감소시킬 수 있을 뿐 아니라 환자의 순응도가 높아 노령 환자들에 대한 처방이 증가하고 있는 상황이다.Currently, anticholinergic agents such as propiberine hydrochloride and oxybutynin hydrochloride are mainly used for the treatment of symptoms of frequent urination, nocturia, and urge incontinence, which can occur in patients with overactive bladder (OAB). , itching, constipation, erythema, and other side effects existing in anticholinergics are caused, and in order to overcome these side effects, Mirabegron, a drug with a mechanism of beta 3 receptor stimulation, is used. Unlike anticholinergic drugs, Mirabegron does not affect the parasympathetic nervous system, so it can reduce the risk of acute urinary retention in the urination phase, and the patient's compliance is high, so the prescription for elderly patients is increasing.

미라베그론의 다양한 합성방법이 제시되었으며, 일 예로, 미국특허 제6,346,532호에서는 하기 반응식 1과 같이 화합물 V를 이용하여 아민기를 보호하고, 니트로페닐을 Pd/C을 사용하여 아미노페놀로 환원시킨 후, 아미노티아졸 유도체와 커플링반응 및 탈보호기 반응을 통해 미라베그론을 합성하였다. 그러나 미국특허 제6,346,532호는 아민을 보호하고, 탈보호하는 공정으로 인해 전체 제조공정이 길어지는 단점이 있으며, 환원반응시 고가의 Pd/C 촉매 및 위험한 수소기체를 사용해야 하는 단점이 있다.Various methods of synthesizing Mirabegron have been proposed. For example, in US Patent No. 6,346,532, an amine group is protected using Compound V as shown in Scheme 1 below, and nitrophenyl is reduced to aminophenol using Pd/C. , mirabegron was synthesized through a coupling reaction with an aminothiazole derivative and a deprotection group reaction. However, US Patent No. 6,346,532 has disadvantages in that the entire manufacturing process is lengthened due to the process of protecting and deprotecting the amine, and there are disadvantages in that an expensive Pd/C catalyst and dangerous hydrogen gas must be used during the reduction reaction.

<반응식 1><Scheme 1>

Figure pat00001
Figure pat00001

미국특허 제7,342,117호는 하기 반응식 2와 같이 화합물 V의 아민을 보호기 없이 바로 환원반응시켜 화합물 VI을 얻고, 이후 아미노티아졸기를 도입하여 미라베그론을 합성하는 개선된 방법을 제시하고 있으나, 이 또한 고가의 귀금속 촉매인 Pd/C 촉매와 위험한 수소기체를 사용해야 하는 단점이 있다.U.S. Patent No. 7,342,117 suggests an improved method for synthesizing mirabegron by directly reducing the amine of Compound V without a protecting group to obtain Compound VI, and then introducing an aminothiazole group as shown in Scheme 2 below, but this also There are disadvantages in that expensive noble metal catalysts such as Pd/C catalysts and dangerous hydrogen gas must be used.

<반응식 2><Scheme 2>

Figure pat00002
Figure pat00002

상기와 같이 제시된 합성법 대부분은 화합물 V(니트로페닐)의 니트로기를 아민으로 환원하는 공정을 거쳐야 한다. 그러나 이 과정에서 유연물질인 하기 화합물 VII이 생성되는데 이 화합물은 미라베그론 합성과정에서 아미노티아졸과 반응하여 하기 화합물 VIII(YM-541570)을 형성하여 새로운 유연물질이 발생하며, YM-541570은 결정화 공정에서 제거가 어려워 최종화합물에 잔류하게 된다. 또한 환원반응에 사용되는 금속촉매 중 일부는 화합물 IX의 키랄성 이성질체의 증가를 야기시킨다.Most of the synthesizing methods suggested above must go through a process of reducing the nitro group of compound V (nitrophenyl) to an amine. However, in this process, the following compound VII is produced. This compound reacts with aminothiazole in the mirabegron synthesis process to form the following compound VIII (YM-541570) to generate a new related substance, YM-541570 It is difficult to remove in the crystallization process and remains in the final compound. In addition, some of the metal catalysts used in the reduction reaction cause an increase in the chiral isomer of compound IX.

Figure pat00003
Figure pat00003

Figure pat00004
Figure pat00004

현재까지 알려진 화합물 V의 니트로 환원반응은 Pd/C, Ranny Ni, Fe, Sn 등의 금속촉매를 사용하는 것이 일반적인 방법이다. 상기와 같은 기술의 단점을 극복하기 위해 개발된 기술로는 중국공개특허 CN103193730 및 CN103232352가 있으며, 이는 하기 반응식 3과 같이 2-(4-아미노페닐)에탄올을 출발물질로 미라베그론을 제조하여 수소반응을 회피하고 키랄성 이성질체의 생성을 억제할 수 있다. 그러나 알코올로부터 알데히드로의 산화반응의 경우 현장 생산 적용에 어려움을 지니고 있으며, 고가의 (R)-2-아미노-1-페닐에탄올을 사용하므로 경제적 단점이 있다.For the nitro reduction reaction of compound V known so far, it is a common method to use a metal catalyst such as Pd/C, Ranny Ni, Fe, or Sn. As a technology developed to overcome the disadvantages of the above technology, there are Chinese Patent Laid-Open Patent CN103193730 and CN103232352, which are produced by preparing mirabegron using 2-(4-aminophenyl)ethanol as a starting material as shown in Reaction Scheme 3 below. The reaction can be avoided and the production of chiral isomers can be suppressed. However, in the case of the oxidation reaction from alcohol to aldehyde, it is difficult to apply to field production, and since expensive (R)-2-amino-1-phenylethanol is used, there is an economic disadvantage.

<반응식 3><Scheme 3>

Figure pat00005
Figure pat00005

대한민국등록특허 제10-1868438호는 상기 단점을 극복하기 위해 하기 반응식 4와 같이, 알킬아민이 카복실 보호기로 치환된 방향족 아민 유도체와 프탈이미드로 치환된 티아졸 유도체를 반응시켜 화합물을 제조하는 단계 및 탈 카복실 보호기 반응 후 탈 프탈이미드 보호기 반응을 거쳐 최종 화합물을 제조하였다. 이는 수소 반응이 포함된 기존 제조방법에 비해 안정적이기는 하지만 보호기 도입과정과 탈보호 과정 등으로 인하여 기존 금속촉매를 이용한 환원반응과 비교하여 반응단계가 길어 경제적이지 못하다.Korean Patent No. 10-1868438 discloses a step of preparing a compound by reacting an aromatic amine derivative in which an alkylamine is substituted with a carboxyl protecting group and a thiazole derivative in which an alkylamine is substituted with a phthalimide as shown in Scheme 4 below to overcome the above disadvantages And after the decarboxyl protecting group reaction, the final compound was prepared through the dephthalimide protecting group reaction. Although this is more stable than the existing manufacturing method including hydrogen reaction, it is not economical because the reaction step is long compared to the reduction reaction using the existing metal catalyst due to the introduction process of the protecting group and the deprotection process.

<반응식 4><Scheme 4>

Figure pat00006
Figure pat00006

본 발명은 종래 미라베그론 합성에 있어 제기된 고가 촉매의 사용, 대량생산에 부적합한 공정문제 및 수소반응 또는 금속촉매를 사용한 환원반응의 문제점을 개선한 후발 기술들의 문제를 더욱 개선하여 상업적인 대량생산에 적합한 경제적인 미라베그론을 제조할 수 있는 미라베그론 중간체 제조방법을 제공하는 것을 목적으로 한다.The present invention is a commercial mass production by further improving the problems of later technologies that have improved the problems of the use of expensive catalysts raised in the conventional synthesis of Mirabegron, the process problems unsuitable for mass production, and the problems of the hydrogen reaction or the reduction reaction using a metal catalyst. An object of the present invention is to provide a method for preparing an intermediate mirabegron capable of producing a suitable and economical mirabegron.

본 발명은 1) 하기 화학식 2로 표시되는 화합물 또는 이의 염을 용매 하에서 수소공여체 물질 및 아연(zinc) 분말과 반응시켜 니트로기를 아민기로 환원시키는 단계;The present invention comprises the steps of: 1) reducing a nitro group to an amine group by reacting a compound represented by the following Chemical Formula 2 or a salt thereof with a hydrogen donor material and zinc powder in a solvent;

<화학식 2><Formula 2>

Figure pat00007
Figure pat00007

2) 상기 1) 단계의 생성물의 pH를 조정하여 추출하는 단계; 및2) extracting by adjusting the pH of the product of step 1); and

3) 상기 2) 단계에서 얻어진 추출물을 결정화하여 하기 화학식 1로 표시되는 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 제조하는 단계;를 포함하는 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 제조방법을 제공한다.3) crystallizing the extract obtained in step 2) to prepare (R)-2-((4-aminophenethyl)amino)-1-phenylethanol represented by the following formula (1); (R) A method for preparing -2-((4-aminophenethyl)amino)-1-phenylethanol is provided.

<화학식 1><Formula 1>

Figure pat00008
Figure pat00008

상기 아연(zinc) 분말은 상기 화학식 2로 표시되는 화합물 중량대비 0.5배 내지 8배로 반응시키는 것을 특징으로 한다.The zinc (zinc) powder is characterized in that the reaction is 0.5 to 8 times the weight of the compound represented by the formula (2).

상기 수소공여체 물질은 암모늄 또는 포스페이트이며, 상기 암모늄은 염화암모늄, 탄산암모늄, 탄산수소암모늄, 인산암모늄, 폼산암모늄 및 황산암모늄으로 이루어진 군에서 선택되는 어느 1종 이상이고, 상기 포스페이트는 모노포타슘포스페이트(Monopotassium phosphate), 디포타슘포스페이트(Dipotassium phosphate), 인산(Phosphoric acid), 모노소듐포스페이트(Monosodium phosphate) 및 디소듐포스페이트(Disodium phosphate)로 이루어진 군에서 선택되는 어느 1종 또는 2종 이상이 혼합된 것을 사용한다.The hydrogen donor material is ammonium or phosphate, and the ammonium is at least one selected from the group consisting of ammonium chloride, ammonium carbonate, ammonium hydrogen carbonate, ammonium phosphate, ammonium formate and ammonium sulfate, and the phosphate is monopotassium phosphate ( Monopotassium phosphate), dipotassium phosphate (Dipotassium phosphate), phosphoric acid (Phosphoric acid), monosodium phosphate (Monosodium phosphate) and disodium phosphate (Disodium phosphate) any one selected from the group consisting of or a mixture of two or more use.

상기 용매는 테트라하이드로퓨란, 아세토니트릴, 아세톤, 에틸아세테이트, 메틸렌클로라이드, 클로로포름 및 물로 이루어진 군에서 선택되는 어느 1종 또는 2종 이상이 혼합된 것을 사용한다.As the solvent, any one or a mixture of two or more selected from the group consisting of tetrahydrofuran, acetonitrile, acetone, ethyl acetate, methylene chloride, chloroform and water is used.

상기 1) 단계에서, 용매 및 수소공여체 물질을 혼합한 용액의 pH는 5 내지 7이며, 0℃ 내지 40℃에서 30분 내지 3시간 동안 수행되는 것을 특징으로 한다.In step 1), the pH of the mixed solution of the solvent and the hydrogen donor material is 5 to 7, and it is characterized in that it is carried out at 0° C. to 40° C. for 30 minutes to 3 hours.

상기 3) 단계는 pH를 9 내지 14로 조정하는 것을 특징으로 한다.Step 3) is characterized in that the pH is adjusted to 9 to 14.

또한, 본 발명은 상기 제조방법으로 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 제조하는 단계; 및 상기 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 2-아미노티아졸-4-일아세트산과 반응시켜 미라베그론을 제조하는 단계;를 포함하는 미라베그론 제조방법을 제공한다.In addition, the present invention comprises the steps of preparing (R)-2-((4-aminophenethyl)amino)-1-phenylethanol by the above preparation method; and reacting (R)-2-((4-aminophenethyl)amino)-1-phenylethanol with 2-aminothiazol-4-ylacetic acid to prepare Mirabegron; Provided is a method for manufacturing a gronn.

본 발명에 따른 제조방법은 현장 생산에서 높은 제조비용 및 낮은 생산효율의 제약을 받는 수소반응을 배제할 수 있고, 손쉽게 구할 수 있는 아연 분말 환원 촉매를 이용하여 부반응물 생성이 없는 높은 순도와 수율을 갖는 고품질의 아미드 유도체를 제조할 수 있으며, 이를 사용하여 특별한 정제과정 없이 고순도, 고수율의 미라베그론을 제조할 수 있다.The manufacturing method according to the present invention can exclude hydrogen reaction, which is constrained by high manufacturing cost and low production efficiency, in on-site production, and uses an easily available zinc powder reduction catalyst to achieve high purity and yield without generating side reactants. It is possible to prepare high-quality amide derivatives having a high-purity, high-yield Mirabegron without a special purification process using this.

도 1은 본 발명의 실시예에 따른 미라베그론의 HPLC 분석 결과를 나타낸 것이다.
도 2는 본 발명의 실시예에 따른 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 HPLC 분석 결과를 나타낸 것이다.
도 3은 본 발명의 실시예에 따른 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 이성질체 확인 HPLC 분석 결과를 나타낸 것이다.
도 4는 비교예 1에 따른 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 HPLC 분석 결과를 나타낸 것이다.
도 5는 비교예 2에 따른 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 HPLC 분석 결과를 나타낸 것이다.
도 6은 비교예 3에 따른 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 이성질체 확인 HPLC 분석 결과를 나타낸 것이다.
1 shows the HPLC analysis results of Mirabegron according to an embodiment of the present invention.
2 shows the results of HPLC analysis of (R)-2-((4-aminophenethyl)amino)-1-phenylethanol according to an embodiment of the present invention.
3 shows the isomer confirmation HPLC analysis result of (R)-2-((4-aminophenethyl)amino)-1-phenylethanol according to an embodiment of the present invention.
4 shows the results of HPLC analysis of (R)-2-((4-aminophenethyl)amino)-1-phenylethanol according to Comparative Example 1. FIG.
5 shows the results of HPLC analysis of (R)-2-((4-aminophenethyl)amino)-1-phenylethanol according to Comparative Example 2. FIG.
6 shows the results of HPLC analysis for isomer confirmation of (R)-2-((4-aminophenethyl)amino)-1-phenylethanol according to Comparative Example 3. FIG.

이하, 본 발명을 보다 상세하게 설명한다. 본 발명을 설명함에 있어, 관련된 공지 구성 또는 기능에 대한 구체적인 설명이 본 발명의 요지를 흐릴 수 있다고 판단되는 경우에는 그 상세한 설명은 생략한다.Hereinafter, the present invention will be described in more detail. In describing the present invention, if it is determined that a detailed description of a related known configuration or function may obscure the gist of the present invention, the detailed description thereof will be omitted.

본 발명은 1) 하기 화학식 2로 표시되는 화합물 또는 이의 염을 용매 하에서 수소공여체 물질 및 아연(zinc) 분말과 반응시켜 니트로기를 아민기로 환원시키는 단계;The present invention comprises the steps of: 1) reducing a nitro group to an amine group by reacting a compound represented by the following Chemical Formula 2 or a salt thereof with a hydrogen donor material and zinc powder in a solvent;

<화학식 2><Formula 2>

Figure pat00009
Figure pat00009

2) 상기 1) 단계의 생성물을 여과 및 세척하여 아연 분말을 제거하는 단계;2) filtering and washing the product of step 1) to remove zinc powder;

3) pH를 조정하여 추출하는 단계; 및3) extracting by adjusting the pH; and

4) 상기 3) 단계에서 얻어진 추출물을 결정화하여 하기 화학식 1로 표시되는 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 제조하는 단계;를 포함하는 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 제조방법을 제공한다.4) crystallizing the extract obtained in step 3) to prepare (R)-2-((4-aminophenethyl)amino)-1-phenylethanol represented by the following formula (1); (R) A method for preparing -2-((4-aminophenethyl)amino)-1-phenylethanol is provided.

<화학식 1><Formula 1>

Figure pat00010
Figure pat00010

상기 1) 단계는 상기 화학식 2의 니트로기를 아민기로 치환하기 위하여, 아연 분말을 상기 화학식 2가 용해되어 있는 용매 및 수소공여체 물질의 혼합용액에 넣고 아민기를 치환시키는 단계이다.Step 1) is a step of substituting an amine group by putting zinc powder in a mixed solution of a solvent in which Formula 2 is dissolved and a hydrogen donor material in order to replace the nitro group of Formula 2 with an amine group.

상기 아연 분말은 상기 화학식 2로 표시되는 화합물 중량대비 0.5배 내지 12배로 반응시키는 것이 바람직하며, 더욱 바람직하게는 0.5매 내지 8배로 반응시키는 것이 좋다. 또한 상기 아연 분말은 급격한 발열에 의한 목적 화합물의 분해 또는 위험성을 방지하기 위하여 서서히 분할 투입하여 적정 온도를 유지하는 것이 바람직하다.The zinc powder is preferably reacted at 0.5 to 12 times the weight of the compound represented by Formula 2, and more preferably 0.5 to 8 times by weight. In addition, in order to prevent decomposition or danger of the target compound due to rapid heat generation, the zinc powder is gradually added in portions to maintain an appropriate temperature.

상기 수소공여체 물질은 암모늄 또는 포스페이트이며, 상기 암모늄은 염화암모늄, 탄산암모늄, 탄산수소암모늄, 인산암모늄, 폼산암모늄 및 황산암모늄으로 이루어진 군에서 선택되는 어느 1종 이상이고, 상기 포스페이트는 모노포타슘포스페이트(Monopotassium phosphate), 디포타슘포스페이트(Dipotassium phosphate), 인산(Phosphoric acid), 모노소듐포스페이트(Monosodium phosphate) 및 디소듐포스페이트(Disodium phosphate)로 이루어진 군에서 선택되는 어느 1종 이상이다.The hydrogen donor material is ammonium or phosphate, and the ammonium is at least one selected from the group consisting of ammonium chloride, ammonium carbonate, ammonium hydrogen carbonate, ammonium phosphate, ammonium formate and ammonium sulfate, and the phosphate is monopotassium phosphate ( Monopotassium phosphate), dipotassium phosphate (Dipotassium phosphate), phosphoric acid (Phosphoric acid), monosodium phosphate (Monosodium phosphate) and disodium phosphate (Disodium phosphate) is any one or more selected from the group consisting of.

이러한 아연 분말을 이용한 반응은 별도의 수소가스가 필요하지 않으며, 고온 고압의 반응조건이 필요하지 않다. 또한 상기에서 언급한 Pd/C, Rani Ni, Fe, SnCl2 등의 사용시 다량으로 발생되는 예상불순물(하기 화합물 VII, 화합물 VIII, 화합물 IX 등)의 생성을 최소화할 수 있다.This reaction using zinc powder does not require a separate hydrogen gas, and does not require high temperature and high pressure reaction conditions. In addition, it is possible to minimize the generation of expected impurities (Compound VII, Compound VIII, Compound IX, etc.) generated in large amounts when using the above-mentioned Pd/C, Rani Ni, Fe, SnCl 2 and the like.

Figure pat00011
Figure pat00011

Figure pat00012
Figure pat00012

상기 용매는 테트라하이드로퓨란, 아세토니트릴, 아세톤, 에틸아세테이트, 메틸렌클로라이드, 클로로포름 및 물로 이루어진 군에서 선택되는 어느 1종 이상인 것이 바람직하다. The solvent is preferably at least one selected from the group consisting of tetrahydrofuran, acetonitrile, acetone, ethyl acetate, methylene chloride, chloroform and water.

또한, 상기 용매 및 수소공여체 물질을 혼합한 용액의 pH는 5 내지 7인 것이 바람직하며, 만약 상기 pH 범위를 벗어나 반응을 진행할 경우, 아연 분말이 용해되거나 또는 수산화아연으로 되어 아연의 제거가 어려울 수 있으며, 또는 아민기로 치환된 화학식 1의 염이 생성되어 목적 화합물을 최대로 얻을 수 없어 수율 저하의 문제가 발생할 수 있다.In addition, the pH of the solution in which the solvent and the hydrogen donor material are mixed is preferably 5 to 7, and if the reaction proceeds outside the above pH range, zinc powder may be dissolved or zinc hydroxide may be difficult to remove. Or, the salt of Formula 1 substituted with an amine group is generated, so that the target compound cannot be maximally obtained, and thus a problem of yield reduction may occur.

상기 1) 단계는 0℃ 내지 40℃에서 30분 내지 3시간 동안 수행되는 것이 바람직하다. 만약 온도가 0℃ 미만이면 1차 환원된 중간체까지 반응이 진행되어 완전한 반응이 이루어지지 않을 수 있으며, 40℃를 초과할 경우 반응속도 및 완결도가 빨라지는 반면, 목적 화합물이 다량 분해되어 수율 및 순도 저하의 문제가 발생할 수 있다.Step 1) is preferably performed at 0° C. to 40° C. for 30 minutes to 3 hours. If the temperature is less than 0 ° C, the reaction proceeds to the primary reduced intermediate and a complete reaction may not be achieved. If the temperature exceeds 40 ° C, the reaction rate and completion rate are accelerated, while the target compound is decomposed in a large amount, resulting in yield and A problem of lowering purity may occur.

또한, 상기 2) 단계에서 세척은 반응에 사용된 유기용매와 물의 혼합용액 또는 물을 사용하여 수행하는 것이 바람직하며, 상기 유기용매는 에틸아세테이트, 부틸아세테이트, 이소부틸아세테이트, 디에틸에테르, 디메틸에테르, 이소프로필에테르, 메틸에틸케톤 또는 디클로로메탄을 포함한다.In addition, the washing in step 2) is preferably performed using a mixed solution or water of the organic solvent and water used for the reaction, and the organic solvent is ethyl acetate, butyl acetate, isobutyl acetate, diethyl ether, dimethyl ether. , isopropyl ether, methyl ethyl ketone or dichloromethane.

상기 3) 단계는 pH를 9 내지 14로 조정하는 것을 특징으로 하며, 암모늄 또는 포스페이트를 제거한다.Step 3) is characterized in that the pH is adjusted to 9 to 14, and ammonium or phosphate is removed.

상기 4) 단계의 결정화 단계는 추출물로부터 농축과정 없이 아민기에 염을 형성하는 단계로, 염산, 황산, 질산, 인산, 아세트산, 포름산, 시트르산, 옥살산, 푸마릭산 또는 벤조산 등을 사용할 수 있으나, 이에 제한되는 것은 아니다.The crystallization step of step 4) is a step of forming a salt with an amine group from the extract without a concentration process, and hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, acetic acid, formic acid, citric acid, oxalic acid, fumaric acid, or benzoic acid may be used, but limited thereto it's not going to be

또한, 본 발명은 상기 제조방법으로 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 제조하는 단계; 및 상기 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 아미노티아졸 유도체와 커플링 반응시켜 미라베그론을 제조하는 단계;를 포함하는 미라베그론 제조방법을 제공한다.In addition, the present invention comprises the steps of preparing (R)-2-((4-aminophenethyl)amino)-1-phenylethanol by the above preparation method; and preparing mirabegron by coupling the (R)-2-((4-aminophenethyl)amino)-1-phenylethanol with an aminothiazole derivative to prepare mirabegron. to provide.

이하에서, 본 발명의 실시예를 들어 구체적으로 설명하지만, 본 발명의 하기 실시예로 한정되는 것은 아니다.Hereinafter, examples of the present invention will be described in detail, but the present invention is not limited to the following examples.

실시예Example 1. (R)-2-((4- 1. (R)-2-((4- 아미노페네틸aminophenethyl )아미노)-1-)amino)-1- 페닐에탄올Phenylethanol (화학식 1) (Formula 1) 합성예Synthesis example

(R)-2-{[2-(4-니트로페닐)에틸]아미노}-1-페닐에탄올-염산염(화학식 2) 10 g을 테트라하이드로퓨란(THF) 25 ㎖에 투입하고, 정제수 80 ㎖를 첨가한 후 염화암모늄(NH4Cl) 10 g을 투입하였다. 아연 분말 20 g을 나누어 첨가한 후 실온에서 1시간 동안 반응시켰다. 반응 종결 후, 여과하여 아연 분말을 제거하였다. 여과액에 초산에틸 50 ㎖를 첨가하고, NaOH 수용액을 가하여 pH를 조절하였다. 수득한 유기층에 진한염산을 투입한 후 0~5℃로 냉각하여 1시간 동안 교반하며 결정화하였다. 생성된 결정을 여과한 후 초산에틸로 세척하고, 실온에서 감압 건조하여 화학식 1을 8.4 g 수득하였다(수율 93%, 순도 99.91%, 화합물 VII 불검출).10 g of (R)-2-{[2-(4-nitrophenyl)ethyl]amino}-1-phenylethanol-hydrochloride (Formula 2) was added to 25 ml of tetrahydrofuran (THF), and 80 ml of purified water was added After the addition, 10 g of ammonium chloride (NH 4 Cl) was added. After adding 20 g of zinc powder in portions, it was reacted at room temperature for 1 hour. After completion of the reaction, the zinc powder was removed by filtration. To the filtrate, 50 ml of ethyl acetate was added, and an aqueous NaOH solution was added to adjust the pH. After adding concentrated hydrochloric acid to the obtained organic layer, it was cooled to 0-5° C. and crystallized with stirring for 1 hour. The resulting crystals were filtered, washed with ethyl acetate, and dried under reduced pressure at room temperature to obtain 8.4 g of Formula 1 (yield 93%, purity 99.91%, compound VII not detected).

실시예Example 2. (R)-2-((4- 2. (R)-2-((4- 아미노페네틸aminophenethyl )아미노)-1-)amino)-1- 페닐에탄올Phenylethanol (화학식 1) (Formula 1) 합성예Synthesis example

(R)-2-{[2-(4-니트로페닐)에틸]아미노}-1-페닐에탄올-염산염(화학식 2) 10 g을 테트라하이드로퓨란(THF) 25 ㎖에 투입하고, 정제수 80 ㎖를 첨가한 후 포타슘포스페이트 모노베이직(KH2PO4) 20 g을 투입하였다. 아연 분말 20 g을 나누어 첨가한 후 실온에서 2시간 동안 반응시켰다. 반응 종결 후, 여과하여 아연 분말을 제거하였다. 여과액에 초산에틸 50 ㎖를 첨가하고, NaOH 수용액을 가하여 pH를 조절하였다. 층 분리하여 유기층을 회수한 후 수득한 유기층에 진한염산을 투입하고, 0~5℃로 냉각하여 1시간 동안 교반하며 결정화하였다. 생성된 결정을 여과 및 실온 감압 건조하여 화학식 1을 8.2 g 수득하였다(수율 90%, 순도 99.85%, 화합물 VII 불검출).10 g of (R)-2-{[2-(4-nitrophenyl)ethyl]amino}-1-phenylethanol-hydrochloride (Formula 2) was added to 25 ml of tetrahydrofuran (THF), and 80 ml of purified water was added After addition, 20 g of potassium phosphate monobasic (KH 2 PO 4 ) was added. After adding 20 g of zinc powder in portions, it was reacted at room temperature for 2 hours. After completion of the reaction, the zinc powder was removed by filtration. To the filtrate, 50 ml of ethyl acetate was added, and an aqueous NaOH solution was added to adjust the pH. After separating the layers to recover the organic layer, concentrated hydrochloric acid was added to the obtained organic layer, cooled to 0-5° C., and crystallized with stirring for 1 hour. The resulting crystals were filtered and dried under reduced pressure at room temperature to obtain 8.2 g of Formula 1 (yield 90%, purity 99.85%, compound VII not detected).

실시예Example 3. 3. 미라베그론Mirabegron 합성예Synthesis example

대한민국등록특허 제10-0908796호의 실시예 1의 방법에 따라 제조하였다.It was prepared according to the method of Example 1 of Korean Patent No. 10-0908796.

(R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올-염산염 8.00 g, 2-아미노티아졸-4-일아세트산 4.32 g, 진한염산 2.64 g 및 물 120 ㎖를 혼합한 후 1-(3-디메틸아미노프로필)-3-에틸카보디이미드-염산염(EDC) 5.76 g을 실온에서 가하여 1시간 동안 교반하였다. 수산화나트륨 2.40 g 및 물 40 ㎖의 혼합액을 상기 반응액에 적가하여 결정화하였다. 여과하여 생성된 결정을 수집한 후 물로 세정하고, 진공건조시켜 미라베그론 10.1 g을 수득하였다(수율 93%, 순도 99.95%, 화합물 VIII 0.02%).(R)-2-((4-aminophenethyl)amino)-1-phenylethanol-hydrochloride 8.00 g, 2-aminothiazol-4-ylacetic acid 4.32 g, concentrated hydrochloric acid 2.64 g, and water 120 ml were mixed. After that, 5.76 g of 1-(3-dimethylaminopropyl)-3-ethylcarbodiimide-hydrochloride (EDC) was added at room temperature and stirred for 1 hour. A mixture of 2.40 g of sodium hydroxide and 40 ml of water was added dropwise to the reaction solution for crystallization. The resulting crystals were collected by filtration, washed with water, and dried under vacuum to obtain 10.1 g of mirabegron (yield 93%, purity 99.95%, compound VIII 0.02%).

비교예comparative example 1 One

국제공개특허 WO2015/155604의 실시예 1의 방법에 따라 제조하였다.It was prepared according to the method of Example 1 of International Patent Publication WO2015/155604.

정제수 85 ㎖에 Fe 10 g과 염산 5.8 g을 투입한 후 (R)-2-{[2-(4-니트로페닐)에틸]아미노}-1-페닐에탄올-염산염 17.0 g과 메탄올 50 ㎖를 첨가하였다. 반응액을 80℃로 승온하여 3시간 동안 반응시켰다. 반응 종결 후 30℃로 냉각하여 Fe를 셀라이트 여과하여 제거하였다. 여과액을 감압 농축한 후 농축액에 초산에틸과 메탄올을 가하여 결정화하였다. 여과하여 생성된 결정을 수집한 후 진공 건조하여 화학식 1을 13.3 g 수득하였다(수율 86%, 순도 98.82%, 화합물 VII 0.19%).After adding 10 g of Fe and 5.8 g of hydrochloric acid to 85 ml of purified water, 17.0 g of (R)-2-{[2-(4-nitrophenyl)ethyl]amino}-1-phenylethanol-hydrochloride and 50 ml of methanol were added. did. The reaction solution was heated to 80° C. and reacted for 3 hours. After completion of the reaction, it was cooled to 30° C. and Fe was removed by celite filtration. After the filtrate was concentrated under reduced pressure, ethyl acetate and methanol were added to the concentrated solution for crystallization. The resulting crystals were collected by filtration and dried under vacuum to obtain 13.3 g of Formula 1 (yield 86%, purity 98.82%, compound VII 0.19%).

비교예comparative example 2 2

Journal of Chemical and Pharmaceutical Research, 2015, 7(4):1473-1478의 미라베그론 제조방법에 따라 제조하였다.It was prepared according to the mirabegron preparation method of Journal of Chemical and Pharmaceutical Research, 2015, 7(4):1473-1478.

반응기에 (R)-2-{[2-(4-니트로페닐)에틸]아미노}-1-페닐에탄올-염산염 12.0 g과 에탄올 130 ㎖를 투입한 후 stannous chloride dehydrate 42.2 g을 천천히 투입하였다. 반응액을 70℃로 승온하여 2시간 동안 반응시켰다. 반응 종결 후 55℃에서 감압 농축하여 에탄올을 제거하였다. 농축한 모액에 포화 탄산수소나트륨 용액 200 ㎖를 투입한 후 초산에틸 200 ㎖로 4회, 10% 메탄올/염화메틸렌 혼합용액 200 ㎖로 2회 추출하였다. 추출 용액을 50℃로 감압 농축한 후 염화메틸렌과 n-핵산을 사용하여 결정화하였다. 여과하여 생성된 결정을 수집한 후 진공 건조하여 화학식 1을 9.1 g 수득하였다(수율 84%, 순도 92.91%, 화합물 VII 0.17%).12.0 g of (R)-2-{[2-(4-nitrophenyl)ethyl]amino}-1-phenylethanol-hydrochloride and 130 ml of ethanol were added to the reactor, and then 42.2 g of stannous chloride dehydrate was slowly added thereto. The reaction solution was heated to 70° C. and reacted for 2 hours. After completion of the reaction, ethanol was removed by concentration under reduced pressure at 55°C. After adding 200 ml of a saturated sodium hydrogen carbonate solution to the concentrated mother liquor, it was extracted 4 times with 200 ml of ethyl acetate and twice with 200 ml of a 10% methanol/methylene chloride mixed solution. The extraction solution was concentrated under reduced pressure at 50° C. and then crystallized using methylene chloride and n-nucleic acid. The resulting crystals were collected by filtration and vacuum dried to obtain 9.1 g of Formula 1 (yield 84%, purity 92.91%, compound VII 0.17%).

비교예comparative example 3 3

대한민국등록특허 제10-0908796호의 참고예 3의 방법에 따라 제조하였다.It was prepared according to the method of Reference Example 3 of Korean Patent Registration No. 10-0908796.

(R)-2-{[2-(4-니트로페닐)에틸]아미노}-1-페닐에탄올-염산염 11.0 g, 메탄올 110 ㎖ 및 습윤 10% 팔라듐-탄소(습윤율 54.2%) 1.20 g을 혼합한 후 수소 분위기하에서 수소의 흡입이 정지될 때까지 교반하였다. 반응액을 여과하여 여과액을 감압 농축하였다. 잔사에 메탄올 40 ㎖을 가하여 40℃에서 용해시키고, 디이소프로필에테르 220 ㎖를 가하여 결정화한 후 20℃에서 하룻밤 교반하였다. 여과하여 생성된 결정을 수집한 후 디이소프로필에테르 30 ㎖로 세정하고, 진공 건조하여 화학식 1을 8.9 g 수득하였다(수율 89%, 순도 99.76%, 화합물 VII 0.04%).(R)-2-{[2-(4-nitrophenyl)ethyl]amino}-1-phenylethanol-hydrochloride 11.0 g, methanol 110 ml and 1.20 g wet 10% palladium-carbon (54.2% wet) are mixed. After that, the mixture was stirred under a hydrogen atmosphere until the suction of hydrogen was stopped. The reaction solution was filtered, and the filtrate was concentrated under reduced pressure. 40 ml of methanol was added to the residue to dissolve it at 40°C, and 220 ml of diisopropyl ether was added thereto for crystallization, followed by stirring at 20°C overnight. The resulting crystals were collected by filtration, washed with 30 ml of diisopropyl ether, and dried under vacuum to obtain 8.9 g of Formula 1 (yield 89%, purity 99.76%, compound VII 0.04%).

하기 표 1은 실시예 1 내지 2 및 비교예 1 내지 3의 합성결과를 나타낸 것이다.Table 1 below shows the synthesis results of Examples 1 to 2 and Comparative Examples 1 to 3.

환원제reducing agent 수율yield 순도water 화합물 VIIcompound VII 화합물 IX compound IX 실시예 1Example 1 Zn(NH4Cl)Zn(NH 4 Cl) 93%93% 99.91%99.91% 불검출non-detection 불검출non-detection 실시예 2Example 2 Zn(KH2PO4)Zn(KH 2 PO 4 ) 91%91% 99.85%99.85% 불검출non-detection 불검출non-detection 비교예 1Comparative Example 1 FeFe 86%86% 98.82%98.82% 0.19%0.19% 불검출non-detection 비교예 2Comparative Example 2 SnCl2 SnCl 2 84%84% 92.91%92.91% 0.17%0.17% 불검출non-detection 비교예 3Comparative Example 3 Pd/CPd/C 89%89% 99.76%99.76% 0.04%0.04% 0.32%0.32%

상기 표 1에서 보듯이, 환원단계에서 환원제의 선택이 중간체 아미노페닐(화학식 1)의 수율 및 순도에 큰 영향을 미치는 것을 알 수 있다. 이 중 주요 불순물인 화합물 VII은 미라베그론 제조과정 중 아미노티아졸과 반응하여 유연물질 YM-541570(화합물 VIII)을 발생시키며, 이 불순물은 결정화 공정에서 제거가 어려워 최종화합물에 잔류를 하게 된다. 본 발명에서 제시한 아연을 사용한 제조방법의 경우 비교예와 다르게 화합물 VII이 생성되지 않아 미라베그론 제조과정에서 별도의 정제 과정이 없이도 고순도의 제품을 제조할 수 있다. 또한 환원반응에 사용되는 금속촉매 중 Pd/C(비교예 3)은 화합물 IX의 키랄성 이성질체가 증가함을 볼 수 있다. 따라서 본 방법의 발명은 비교예의 방법보다 우수하며, 종래 미라베그론을 합성하는데 있어 제기된 고가의 촉매 사용과 대량생산에 부적합한 공정문제와 수소반응 또는 금속촉매를 사용한 환원반응의 문제점을 개선한 후발 기술들의 문제를 더욱 개선하여 상업적인 대량생산에 적합한 경제적인 제조방법을 제공한다. As shown in Table 1, it can be seen that the selection of the reducing agent in the reduction step greatly affects the yield and purity of the intermediate aminophenyl (Formula 1). Among them, compound VII, a major impurity, reacts with aminothiazole during the manufacturing process of mirabegron to generate a related substance YM-541570 (compound VIII), and this impurity remains in the final compound because it is difficult to remove in the crystallization process. In the case of the manufacturing method using zinc presented in the present invention, unlike the comparative example, compound VII is not produced, so that a high-purity product can be manufactured without a separate purification process in the mirabegron manufacturing process. In addition, it can be seen that Pd/C (Comparative Example 3) among the metal catalysts used for the reduction reaction increases the chiral isomer of compound IX. Therefore, the invention of the present method is superior to the method of the comparative example, and the problem of the use of expensive catalysts raised in synthesizing Mirabegron and the process problems that are not suitable for mass production and the problems of the reduction reaction using a hydrogen reaction or a metal catalyst are improved after improving By further improving the problems of the techniques, an economical manufacturing method suitable for commercial mass production is provided.

이상, 본 발명을 예시적으로 설명하였으며, 본 발명이 속하는 기술분야에서 통상의 지식을 가지는 자라면 본 발명의 본질적인 특성에서 벗어나지 않는 범위에서 다양한 변형이 가능할 것이다. 따라서, 본 명세서에 개시된 실시예들은 본 발명을 한정하기 위한 것이 아니라 설명하기 위한 것이고, 이러한 실시예에 의하여 본 발명의 사상과 범위가 한정되는 것은 아니다. 본 발명의 보호범위는 아래의 청구범위에 의해서 해석되어야 하며, 그와 동등한 범위 내에 있는 모든 기술은 본 발명의 권리범위에 포함하는 것으로 해석되어야 할 것이다.Above, the present invention has been described by way of example, and various modifications will be possible without departing from the essential characteristics of the present invention by those of ordinary skill in the art to which the present invention pertains. Accordingly, the embodiments disclosed in this specification are intended to illustrate, not to limit the present invention, and the spirit and scope of the present invention are not limited by these embodiments. The protection scope of the present invention should be construed by the following claims, and all technologies within the scope equivalent thereto should be construed as being included in the scope of the present invention.

Claims (10)

1) 하기 화학식 2로 표시되는 화합물 또는 이의 염을 용매 하에서 수소공여체 물질 및 아연(zinc) 분말과 반응시켜 니트로기를 아민기로 환원시키는 단계;
<화학식 2>
Figure pat00013

2) 상기 1) 단계의 생성물을 여과 및 세척하여 아연 분말을 제거하는 단계;
3) pH를 조정하여 추출하는 단계; 및
4) 상기 3) 단계에서 얻어진 추출물을 결정화하는 단계;를 포함하는 하기 화학식 1로 표시되는 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올의 제조방법
<화학식 1>
Figure pat00014

1) reducing a nitro group to an amine group by reacting a compound represented by the following Chemical Formula 2 or a salt thereof with a hydrogen donor material and zinc powder in a solvent;
<Formula 2>
Figure pat00013

2) filtering and washing the product of step 1) to remove zinc powder;
3) extracting by adjusting the pH; and
4) A method for producing (R)-2-((4-aminophenethyl)amino)-1-phenylethanol represented by the following formula (1) comprising a; crystallizing the extract obtained in step 3)
<Formula 1>
Figure pat00014

제1항에 있어서, 상기 아연(zinc) 분말은 상기 화학식 2로 표시되는 화합물 중량대비 0.5배 내지 8배로 반응시키는 것을 특징으로 하는 제조방법
The method according to claim 1, wherein the zinc powder is reacted with 0.5 to 8 times the weight of the compound represented by Formula 2
제1항에 있어서, 상기 수소공여체 물질은 염화암모늄, 탄산암모늄, 탄산수소암모늄, 인산암모늄, 폼산암모늄 및 황산암모늄으로 이루어진 군에서 선택되는 어느 1종 또는 2종 이상 혼합한 것을 특징으로 하는 제조방법
The method according to claim 1, wherein the hydrogen donor material is any one selected from the group consisting of ammonium chloride, ammonium carbonate, ammonium hydrogen carbonate, ammonium phosphate, ammonium formate and ammonium sulfate, or a mixture of two or more types.
제1항에 있어서, 상기 수소공여체 물질은 모노포타슘포스페이트(Monopotassium phosphate), 디포타슘포스페이트(Dipotassium phosphate), 인산(Phosphoric acid), 모노소듐포스페이트(Monosodium phosphate) 및 디소듐포스페이트(Disodium phosphate)로 이루어진 군에서 선택되는 어느 1종 또는 2종 이상 혼합한 것을 특징으로 하는 제조방법
According to claim 1, wherein the hydrogen donor material is monopotassium phosphate (Monopotassium phosphate), dipotassium phosphate (Dipotassium phosphate), phosphoric acid (Phosphoric acid), monosodium phosphate (Monosodium phosphate) and disodium phosphate (Disodium phosphate) consisting of Any one selected from the group or a manufacturing method characterized in that two or more types are mixed
제1항에 있어서, 상기 용매는 테트라하이드로퓨란, 아세토니트릴, 아세톤, 에틸아세테이트, 메틸렌클로라이드, 클로로포름 및 물로 이루어진 군에서 선택되는 어느 1종 또는 2종 이상 혼합한 것을 특징으로 하는 제조방법
The method according to claim 1, wherein the solvent is any one or two or more selected from the group consisting of tetrahydrofuran, acetonitrile, acetone, ethyl acetate, methylene chloride, chloroform and water.
제1항에 있어서, 상기 1) 단계에서 용매 및 수소공여체 물질을 혼합한 용액의 pH는 5 내지 7인 것을 특징으로 하는 제조방법
The method according to claim 1, wherein the pH of the solution in which the solvent and the hydrogen donor material are mixed in step 1) is 5 to 7
제1항에 있어서, 상기 1) 단계는 0℃ 내지 40℃에서 반응시키는 것을 특징으로 하는 제조방법
The method according to claim 1, wherein in step 1), the reaction is performed at 0°C to 40°C.
제1항에 있어서, 상기 1) 단계의 반응시간은 30분 내지 3시간인 것을 특징으로 하는 제조방법
The method according to claim 1, wherein the reaction time of step 1) is 30 minutes to 3 hours.
제1항에 있어서, 상기 3) 단계는 pH를 9 내지 14로 조정하는 것을 특징으로 하는 제조방법
The method according to claim 1, wherein in step 3), the pH is adjusted to 9 to 14.
제1항 내지 제9항 중 어느 한 항에 따른 제조방법에 의해 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 제조하는 단계; 및 상기 (R)-2-((4-아미노페네틸)아미노)-1-페닐에탄올을 2-아미노티아졸-4-일아세트산과 반응시키는 단계;를 포함하는 미라베그론 제조방법

(R)-2-((4-aminophenethyl)amino)-1-phenylethanol by the preparation method according to any one of claims 1 to 9; and reacting (R)-2-((4-aminophenethyl)amino)-1-phenylethanol with 2-aminothiazol-4-ylacetic acid;

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