CN110818578A - Catalytic hydrogenation synthesis method of chiral aminobutanol - Google Patents

Catalytic hydrogenation synthesis method of chiral aminobutanol Download PDF

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Publication number
CN110818578A
CN110818578A CN201911029916.9A CN201911029916A CN110818578A CN 110818578 A CN110818578 A CN 110818578A CN 201911029916 A CN201911029916 A CN 201911029916A CN 110818578 A CN110818578 A CN 110818578A
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chiral
aminobutanol
acid
catalytic hydrogenation
synthesis method
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CN201911029916.9A
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姚琪
谢权
黄琼淋
曾永康
张之翔
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Kaili Catalyst New Materials Co Ltd
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Kaili Catalyst New Materials Co Ltd
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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
    • C07C213/06Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton from hydroxy amines by reactions involving the etherification or esterification of hydroxy groups
    • 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
    • C07C213/10Separation; Purification; Stabilisation; Use of additives
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a catalytic hydrogenation synthesis method of chiral aminobutanol, which directly obtains the chiral aminobutanol by taking chiral aminobutyric acid as a raw material and performing catalytic hydrogenation by using a noble metal catalyst in the presence of protonic acid and a polar solvent. According to the invention, a noble metal catalyst is used as a reducing agent, the catalyst can be recycled, and the chiral aminobutyric acid is completely reduced into the chiral aminobutanol by reacting in a polar solvent system, so that the aminobutanol with high purity and high optical purity is synthesized.

Description

Catalytic hydrogenation synthesis method of chiral aminobutanol
Technical Field
The invention belongs to the technical field of synthesis of medical intermediates, and particularly relates to a synthesis method of chiral aminobutanol.
Background
The (S) -2-aminobutanol is an important intermediate for synthesizing ethambutol hydrochloride which is an antituberculosis drug, and the ethambutol hydrochloride has obvious curative effect on various tuberculosis which is popular at present, including pulmonary tuberculosis and extrapulmonary tuberculosis. The medicament has the obvious characteristics of remarkable medicinal effect, treatment effect on tuberculosis without effect of other medicaments, stronger selective inhibition effect on tubercle bacillus and no drug resistance of tubercle bacillus in a patient to other medicaments.
(R) -3-aminobutanol is an important intermediate for synthesizing new anti-HIV/AIDS drug Lutelvir. Dolutegravir is a human immunodeficiency virus type 1(HIV1) integrase chain transfer inhibitor (INSTI), is used for treating HIV1 infection together with other antiretroviral drugs, and clinical research results show that the dolutegravir is low in toxicity, free of genotoxicity and carcinogenic toxicity, free of obvious fertility toxicity and teratogenicity toxicity when the clinical dosage is 27 times larger than the clinical dosage, strong in HIV1 virus resistance activity is shown by in vitro and in vivo test researches, and safety and tolerance are good.
Various overseas research institutions and enterprises have a certain degree of research on the synthesis of ethambutol hydrochloride, but have strict patent protection, while at present, the domestic research is less, and the domestic demand for the medicine is mainly met by import; therefore, the research on the synthesis process of ethambutol hydrochloride finds a synthesis route which has lower cost and simpler steps, can meet the industrial requirements, and is very important for developing a new process for autonomously synthesizing the medicine in China.
Disclosure of Invention
In view of the above, the main objective of the present invention is to provide a catalytic hydrogenation synthesis method of chiral aminobutanol.
In order to achieve the purpose, the technical scheme of the invention is realized as follows:
chiral aminobutyric acid is used as a raw material, and is directly subjected to catalytic hydrogenation by a noble metal catalyst in the presence of protonic acid and a polar solvent to obtain chiral aminobutanol.
Compared with the prior art, the invention adopts the noble metal catalyst as the reducing agent, the catalyst can be recycled and reacted in a polar solvent system, and the chiral aminobutyric acid is completely reduced into the chiral aminobutanol, thereby synthesizing the aminobutanol with high purity and high optical purity.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail with reference to the following embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
The embodiment of the invention provides a catalytic hydrogenation synthesis method of chiral aminobutanol, which directly obtains the chiral aminobutanol by taking chiral aminobutanoic acid as a raw material and performing catalytic hydrogenation by using a noble metal catalyst in the presence of protonic acid and a polar solvent.
Specifically, chiral aminobutyric acid, a noble metal catalyst, protonic acid and a polar solvent are added into a hydrogenation reaction kettle in batches, the mixture is heated to 50-150 ℃, the pressure is kept at 1.0-10 MPa, the mixture is sampled and analyzed after 2-10 hours, after the reaction is determined, the noble metal catalyst is filtered, filtrate is collected, 1.5 eq-5.5 eq of solid sodium hydroxide is added into the filtrate, 1V-5V of the polar organic solvent is added, the mixture is stirred, stood and layered, the lower layer is continuously and repeatedly extracted, the upper layer is collected, the operation is repeated for three times, the collected upper layer organic phase is firstly distilled to remove the polar organic solvent, and the chiral aminobutanol is obtained through reduced pressure distillation.
The mass ratio of the chiral aminobutyric acid to the noble metal catalyst to the polar solvent is 1: (0.05-0.5): (1-20).
The chiral aminobutyric acid is one or a mixture of at least two of (R) -2-aminobutyric acid, (R) -3-aminobutyric acid, (R) -4-aminobutyric acid, (S) -2-aminobutyric acid, (S) -3-aminobutyric acid and (S) -4-aminobutyric acid.
The protonic acid is one or a mixture of at least two of phosphoric acid, sulfuric acid, hydrochloric acid, trifluoroacetic acid and the like.
The polar solvent is one or a mixture of at least two of methanol, ethanol, isopropanol and water.
The noble metal catalyst is a ruthenium-or rhodium-based catalyst.
Example 1
The embodiment 1 of the invention provides a catalytic hydrogenation synthesis method of (S) -2-aminobutanol, which comprises the steps of adding 70 g of (S) -2-aminobutanol, 400 g of water and 220g of sulfuric acid into a 1L hydrogenation reaction kettle in batches, heating to 95-100 ℃, keeping the pressure at 5Mpa for 10 hours, then sampling and analyzing, after the reaction is finished, filtering a noble metal catalyst, collecting filtrate, adding 40g of solid sodium hydroxide into the filtrate, adding 140ml of anhydrous methanol, stirring, standing, layering, continuously and repeatedly extracting the lower layer, collecting the upper layer, repeating the operation for three times, distilling the collected upper layer organic phase to remove a polar organic solvent, and then carrying out reduced pressure distillation to obtain the chiral aminobutanol with higher purity.
The purity of the aminobutanol synthesized in example 1 of the present invention was 99%, the mass was 54.4g, and the molar yield was 90%.
Example 2
The embodiment 2 of the invention provides a catalytic hydrogenation synthesis method of (S) -3-aminobutanol, which comprises the steps of adding 70 g of (S) -2-aminobutanol, 400 g of water and 220g of sulfuric acid into a 1L hydrogenation reaction kettle in batches, heating to 95-100 ℃, keeping the pressure at 5Mpa for 10 hours, then sampling and analyzing, after the reaction is finished, filtering a noble metal catalyst, collecting filtrate, adding 40g of solid sodium hydroxide into the filtrate, adding 140ml of anhydrous methanol, stirring, standing, layering, continuously and repeatedly extracting the lower layer, collecting the upper layer, repeating the operation for three times, distilling the collected upper layer organic phase to remove a polar organic solvent, and then carrying out reduced pressure distillation to obtain the chiral aminobutanol with higher purity.
The chromatographic purity of the aminobutanol synthesized in the example 2 of the invention is 99%, the mass is 55g, and the molar yield is 91%.
Example 3
The embodiment 3 of the invention provides a catalytic hydrogenation synthesis method of (S) -4-aminobutanol, which comprises the steps of adding 70 g of (S) -2-aminobutanol, 400 g of water and 220g of sulfuric acid into a 1L hydrogenation reaction kettle in batches, heating to 95-100 ℃, keeping the pressure at 5Mpa for 10 hours, then sampling and analyzing, after the reaction is finished, filtering a noble metal catalyst, collecting filtrate, adding 40g of solid sodium hydroxide into the filtrate, adding 140ml of anhydrous methanol, stirring, standing, layering, continuously and repeatedly extracting the lower layer, collecting the upper layer, repeating the operation for three times, distilling the collected upper layer organic phase to remove a polar organic solvent, and then carrying out reduced pressure distillation to obtain the chiral aminobutanol with higher purity.
The purity of the aminobutanol synthesized in example 3 of the present invention was 99%, and the molar yield was 89.4% or more, when the mass was 54 g.
Example 4
The embodiment 4 of the invention provides a catalytic hydrogenation synthesis method of (R) -2-aminobutanol, which comprises the steps of adding 70 g of (S) -2-aminobutanol, 400 g of water and 220g of phosphoric acid into a 1L hydrogenation reaction kettle in batches, heating to 95-100 ℃, keeping the pressure at 5Mpa for 10 hours, then sampling and analyzing, after the reaction is finished, filtering a noble metal catalyst, collecting filtrate, adding 80g of solid sodium hydroxide into the filtrate, adding 140ml of anhydrous methanol, stirring, standing, layering, continuously and repeatedly extracting the lower layer, collecting the upper layer, repeating the operation for three times, distilling the collected upper layer organic phase to remove a polar organic solvent, and then carrying out reduced pressure distillation to obtain the chiral aminobutanol with higher purity.
The purity of the aminobutanol synthesized in example 4 of the present invention was 99%, the mass was 54.4g, and the molar yield was 90%.
Example 5
The embodiment 5 of the invention provides a catalytic hydrogenation synthesis method of (R) -3-aminobutanol, which comprises the steps of adding 70 g of (S) -2-aminobutanol, 400 g of water and 220g of phosphoric acid into a 1L hydrogenation reaction kettle in batches, heating to 95-100 ℃, keeping the pressure at 5Mpa for 10 hours, then sampling and analyzing, filtering a noble metal catalyst after the reaction is finished, collecting filtrate, adding 80g of solid sodium hydroxide into the filtrate, adding 140ml of anhydrous methanol, stirring, standing, layering, continuously and repeatedly extracting the lower layer, collecting the upper layer, repeating the operation for three times, distilling the collected upper layer organic phase to remove a polar organic solvent, and carrying out reduced pressure distillation to obtain the chiral aminobutanol with higher purity.
The purity of the aminobutanol synthesized in example 5 of the present invention was 99%, the mass was 55g, and the molar yield was 91%.
Example 6
The embodiment 6 of the invention provides a catalytic hydrogenation synthesis method of (R) -4-aminobutanol, which comprises the steps of adding 70 g of (S) -2-aminobutanol, 400 g of water and 220g of phosphoric acid into a 1L hydrogenation reaction kettle in batches, heating to 95-100 ℃, keeping the pressure at 5Mpa for 10 hours, then sampling and analyzing, after the reaction is finished, filtering a noble metal catalyst, collecting filtrate, adding 80g of solid sodium hydroxide into the filtrate, adding 140ml of anhydrous methanol, stirring, standing, layering, continuously and repeatedly extracting the lower layer, collecting the upper layer, repeating the operation for three times, distilling the collected upper layer organic phase to remove a polar organic solvent, and then carrying out reduced pressure distillation to obtain the chiral aminobutanol with higher purity.
The amino butanol synthesized in example 6 of the present invention had an optical purity of 99%, a mass of 54g, and a molar yield of 89.4%.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the scope of the present invention.

Claims (7)

1. A catalytic hydrogenation synthesis method of chiral aminobutanol is characterized in that: chiral aminobutyric acid is used as a raw material, and is directly subjected to catalytic hydrogenation by a noble metal catalyst in the presence of protonic acid and a polar solvent to obtain chiral aminobutanol.
2. The catalytic hydrogenation synthesis method of chiral aminobutanol according to claim 1, characterized in that chiral aminobutyric acid, noble metal catalyst, protonic acid and polar solvent are added into a hydrogenation reaction kettle in batches, the mixture is heated to 50-150 ℃ and kept at 1.0-10 Mpa, sampling analysis is carried out after 2-10 hours, after the reaction is determined, the noble metal catalyst is filtered, filtrate is collected, 1.5 eq-5.5 eq of solid sodium hydroxide is added into the filtrate, 1V-5V of polar organic solvent is added, stirring, standing and layering are carried out, the lower layer is continuously extracted repeatedly, the upper layer is collected and repeated for three times, the collected upper layer organic phase is distilled to remove the polar organic solvent, and the chiral aminobutanol is obtained through reduced pressure distillation.
3. The catalytic hydrogenation synthesis method of chiral aminobutanol according to claim 1 or 2, wherein the mass ratio of the chiral aminobutanol to the noble metal catalyst to the polar solvent is 1: (0.05-0.5): (1-20).
4. The catalytic hydrogenation synthesis method of chiral amino butanol according to claim 3, wherein the chiral amino butyric acid is one or a mixture of at least two of (R) -2-aminobutyric acid, (R) -3-aminobutyric acid, (R) -4-aminobutyric acid, (S) -2-aminobutyric acid, (S) -3-aminobutyric acid, (S) -4-aminobutyric acid).
5. The catalytic hydrogenation synthesis method of chiral amino butanol according to claim 4, wherein the protonic acid is a mixture of at least two of phosphoric acid, sulfuric acid, hydrochloric acid, trifluoroacetic acid, and the like.
6. The catalytic hydrogenation synthesis method of chiral amino butanol according to claim 5, wherein the polar solvent is a mixture of at least two of methanol, ethanol, isopropanol and water.
7. The catalytic hydrogenation synthesis method of chiral aminobutanol according to claim 6, characterized in that the noble metal catalyst is a ruthenium-or rhodium-based catalyst.
CN201911029916.9A 2019-10-25 2019-10-25 Catalytic hydrogenation synthesis method of chiral aminobutanol Pending CN110818578A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113336655A (en) * 2020-12-30 2021-09-03 江西迪赛诺制药有限公司 Preparation method of (R) -3-aminobutanol
CN114573463A (en) * 2022-03-23 2022-06-03 江西宇能制药股份有限公司 Preparation method of R-3-aminobutanol

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3953512A (en) * 1973-03-20 1976-04-27 Polska Akademia Nauk Instytut Chemii Organicznej Process for manufacturing 2-aminobutanol
CN101298050A (en) * 2008-07-07 2008-11-05 上虞市众昌化工有限公司 Method for preparing alpha-alkamine using alpha-aminoacid as raw material and used catalyst and preparation of catalyst
CN103769211A (en) * 2014-01-24 2014-05-07 淮北新兴实业有限责任公司 Preparation method of organic-inorganic hybrid material ruthenium-loaded catalyst for synthesizing L-alaninol
CN105061224A (en) * 2015-06-29 2015-11-18 浙江华义医药有限公司 Synthetic method of L-2-aminobutanol
CN105481703A (en) * 2016-01-13 2016-04-13 江西仙康药业有限公司 Method for synthesizing (S)-2-aminobutanol
CN106563487A (en) * 2016-10-28 2017-04-19 绍兴文理学院 Catalyst, preparation method and application thereof
CN107011186A (en) * 2017-03-31 2017-08-04 浙江工业大学 The method of one kind catalysis S (+) 2 aminobutyric acid hydrogenation synthesis S (+) 2 amino butanol
CN108689866A (en) * 2017-04-06 2018-10-23 成都博腾药业有限公司 A kind of synthetic method of (R) -3- amino butanols
CN109970580A (en) * 2019-04-26 2019-07-05 浙江永太科技股份有限公司 A kind of extraction preparation method of R-3- amino butanol

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3953512A (en) * 1973-03-20 1976-04-27 Polska Akademia Nauk Instytut Chemii Organicznej Process for manufacturing 2-aminobutanol
CN101298050A (en) * 2008-07-07 2008-11-05 上虞市众昌化工有限公司 Method for preparing alpha-alkamine using alpha-aminoacid as raw material and used catalyst and preparation of catalyst
CN103769211A (en) * 2014-01-24 2014-05-07 淮北新兴实业有限责任公司 Preparation method of organic-inorganic hybrid material ruthenium-loaded catalyst for synthesizing L-alaninol
CN105061224A (en) * 2015-06-29 2015-11-18 浙江华义医药有限公司 Synthetic method of L-2-aminobutanol
CN105481703A (en) * 2016-01-13 2016-04-13 江西仙康药业有限公司 Method for synthesizing (S)-2-aminobutanol
CN106563487A (en) * 2016-10-28 2017-04-19 绍兴文理学院 Catalyst, preparation method and application thereof
CN107011186A (en) * 2017-03-31 2017-08-04 浙江工业大学 The method of one kind catalysis S (+) 2 aminobutyric acid hydrogenation synthesis S (+) 2 amino butanol
CN108689866A (en) * 2017-04-06 2018-10-23 成都博腾药业有限公司 A kind of synthetic method of (R) -3- amino butanols
CN109970580A (en) * 2019-04-26 2019-07-05 浙江永太科技股份有限公司 A kind of extraction preparation method of R-3- amino butanol

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113336655A (en) * 2020-12-30 2021-09-03 江西迪赛诺制药有限公司 Preparation method of (R) -3-aminobutanol
CN114573463A (en) * 2022-03-23 2022-06-03 江西宇能制药股份有限公司 Preparation method of R-3-aminobutanol

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Application publication date: 20200221