CN1569815A - Amino acid racemization method - Google Patents

Amino acid racemization method Download PDF

Info

Publication number
CN1569815A
CN1569815A CN 200410018050 CN200410018050A CN1569815A CN 1569815 A CN1569815 A CN 1569815A CN 200410018050 CN200410018050 CN 200410018050 CN 200410018050 A CN200410018050 A CN 200410018050A CN 1569815 A CN1569815 A CN 1569815A
Authority
CN
China
Prior art keywords
amino acid
racemization
acid
tyrosine
racemization method
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN 200410018050
Other languages
Chinese (zh)
Other versions
CN1228311C (en
Inventor
何佺
彭阳峰
胡敏杰
赵红亮
付志强
郑艳
Original Assignee
何佺
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 何佺 filed Critical 何佺
Priority to CN 200410018050 priority Critical patent/CN1228311C/en
Publication of CN1569815A publication Critical patent/CN1569815A/en
Application granted granted Critical
Publication of CN1228311C publication Critical patent/CN1228311C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Disclosed is an amino acid racemization method which consists of dissolving the L-amino acid in organic acid solvent, acylating with organic acid anhydride, thus achieving a L-amino racemization ratio of 100% with a fast reaction speed and high yield, the acid anhydride and organic acid solvent can be reclaimed for circulation use.

Description

The amino acid racemization method
Technical field
The present invention relates to amino acid whose a kind of racemization method, specifically be to use chemical process to produce racemic DL-amino acid.
Background technology
So-called racemization is meant optically active compounds generation part change of configuration, is transformed into the process of the steric isomer that does not have opticity.Amino acid is important chipal compounds, has natural L type and two kinds of configurations of non-natural D type, and under certain condition, all or part of process that changes into racemic modification (DL type) of a certain configuration is called the Racemization of Amino Acids effect.L-amino acid is a kind of natural amino acid, the amino acid that promptly usually said human body is necessary, and its performance is familiar with by people very early, has in fields such as medicine, food, chemical industry so far quite widely to use.Along with going deep into of scientific research in the last few years, it is found that the D-amino acid of thinking useless in the past, have the irreplaceable effect of L-amino acid in vital movement and the medication preparation.Non-natural D-amino acid has become the useful especially chiral source of a class, can synthesize a series of chiral drugs with special efficacy with it as chiral precurser.
In industrial production, the racemization of utilization L-amino acid prepares DL-amino acid, is the important channel that obtains D-amino acid single enantiomer through fractionation again.For L-amino acid, there is a large amount of production in China, wide material sources, so racemization technology is very crucial.Even utilize the DL amino acid of chemosynthesis, again through fractionation obtain D-amino acid single enantiomer technological process, in order to improve utilization ratio of raw materials, the L-amino acid after the fractionation still needs further to utilize after the racemization again, and therefore the amino acid racemization method of research and development practicality is significant.
The amino acid Study on Racemization situation of home and abroad existence at present is as follows:
Document (Fang Baiying, Feng Dayan. necessary amino acid racemization Study on Theory and nutrient protein science [J] .1997,18 (8): 12-17) amino acid has been carried out heating racemization under the alkaline condition, most of amino acid racemization rates are between 10-50%.
Document (Sasaji I., et al.US 3213106,1965) is in the pipe of sealing, and 150~250 ℃ and water heat together 12 seed amino acids is carried out the racemization experiment, and racemization has in various degree taken place most of amino acid.Document (Yamada Y, Hongo C, Yoshioka R..Method for the racemization ofoptically active amino acid[J] .J Org Chem.1983,48:843-846.) in the organic acid, racemization under the aldehyde catalyst action.
CN1034183C proposes a kind of acylamino acid recemase of using, and near neutral water racemize N-acyl-alpha--amino acid only at ordinary times, it combines application with D or L acidylate amidohydrolase and makes DL-acyl-alpha--aminocarboxylic production optically-active D or L-alpha amino acid at PH.This method is used two kinds of enzymes, because the specificity of enzyme and losing activity easily is difficult to widespread usage.
Summary of the invention
The objective of the invention is defective, research and develop a kind of chemical racemization method, make the optically active amino acid of tool become racemic DL-amino acid at the various racemization methods of present amino acid.
The technical solution used in the present invention is that the amino acid racemization method is dissolved in L-amino acid in the organic acid solvent, adds organic acid anhydride, heats acidylate takes place, and generates the amido-carboxylic acid of racemization, handles generating DL amino acid through the deacylated tRNA base
In the above-mentioned reaction, racemization occurs in the aminoacyl amination stage, destroyed the rock steady structure of chirality alpha-carbon, form carbanion, after alpha-carbon negative ion (Csp3) forms, because electron density is bigger on the carbon atom, so it is unstable, easily shift to carbonylic carbon atom, resonance is reset to there not to be the carbon alcohol configuration (Csp2) of chirality feature, thereby has realized Racemization of Amino Acidsization.
The R of above-mentioned reaction represent aliphatics, aromatic series and heterocyclic group because of.As Threonine, Xie Ansuan, Isoleucine, Methionin, halfcystine, phenylalanine, tyrosine and proline(Pro) etc.
In the above-mentioned reaction, organic acid solvent is an anhydrous acetic acid, and organic acid anhydride is a diacetyl oxide, and mineral acid is a hydrochloric acid, and basic solution is a sodium hydroxide solution.
Marked improvement of the present invention and beneficial effect are the places: some amino acid, tyrosine for example, racemization chemically is a kind of of comparison difficulty in amino acid, and many racemization methods that other amino acid is suitable for are used for tyrosine, all do not obtain good racemization effect.The present invention adopts the method for acetic anhydride acylation racemization in pure acetic acid solvent, makes the racemization rate 100% of L-tyrosine.And then this method is applied to other amino acid, also obtained good racemization effect.The method of this monoamino-acid racemization has that racemization is complete, speed of response is fast, product yield is high, acid anhydrides and organic acid solvent can recycle and reuse, low cost and other advantages, has actual application value.This racemization method comprises that to most amino acid L-tyrosine, L-proline(Pro), L-Threonine, L-Xie Ansuan, L-Methionin, L-halfcystine, L-phenylalanine, L-Isoleucine all are suitable for.
Embodiment
Embodiment one: add 20gL-tyrosine in the there-necked flask of 250ml, 100ml Glacial acetic acid and 22ml diacetyl oxide stir, and oil bath is heated to 110 ℃.The initial time of record heating, system clarification after 10 minutes.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 10 minutes sampling 10ml surveys its optical value until being 0.Tyrosine reaches 100% racemization, and the required racemization time is 30min.
The solution decompression distillation removes and desolvates after the racemization that obtains, and obtains the thick material of burgundy, adds 100ml3NHCl solution, refluxes two hours, makes the ethanoyl complete hydrolysis.Be about 3 with sodium hydroxide solution regulator solution pH value, add activated carbon decolorizing, remove by filter gac, continue the iso-electric point (pH ≈ 5~6) of dropping sodium solution to DL-tyrosine, filter, drying obtains flaxen DL-tyrosine.Yield is 90% (is that benchmark calculates with raw material L-tyrosine).
Embodiment two: add 20gL-tyrosine in the there-necked flask of 250ml, 100ml Glacial acetic acid and 22ml diacetyl oxide stir, and oil bath is heated to 100 ℃.The initial time of record heating, after 40 minutes, the system clarification.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 10 minutes sampling 10ml surveys its optical value until being 0.Tyrosine reaches 100% racemization, and the required racemization time is 60min.
Embodiment three: add 20gL-tyrosine in the there-necked flask of 250ml, 100ml Glacial acetic acid and 22ml diacetyl oxide stir, and oil bath is heated to 80 ℃.The initial time of record heating, system clarification after 80 minutes.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 30 minutes sampling 10ml surveys its optical value until being 0.Tyrosine reaches 100% racemization, and the required racemization time is 140min.
Embodiment four: add 20gL-tyrosine in the there-necked flask of 250ml, 100ml Glacial acetic acid and 33ml diacetyl oxide stir, and oil bath is heated to 80 ℃.The initial time of record heating, treated the system clarification in 70 minutes after.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 10 minutes sampling 10ml surveys its optical value until being 0.Tyrosine reaches 100% racemization, and the required racemization time is 90min.
Embodiment five: add 20gL-tyrosine in the there-necked flask of 250ml, 100ml Glacial acetic acid and 15.6ml diacetyl oxide stir, and oil bath is heated to 80 ℃.The initial time of record heating, treated the system clarification in 120 minutes after.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 1 hour sampling 10ml surveys its optical value until being 0.Tyrosine reaches 100% racemization, and the required racemization time is 600min.
Embodiment six: add the 10.36gL-proline(Pro) in the there-necked flask of 250ml, 75ml Glacial acetic acid and 18ml diacetyl oxide stir, and oil bath is heated to 100 ℃.The initial time of record heating, after 10 minutes, proline(Pro) dissolves fully, and the system clear is got the 10ml sample, is diluted to 25ml with deionized water and surveys its optical value.After this every mistake 10 minutes sampling 10ml surveys its optical value until being 0.Proline(Pro) reaches 100% racemization, and the required racemization time is 60min.
Embodiment seven: add the 16.07gL-Threonine in the there-necked flask of 250ml, 75ml Glacial acetic acid and 40ml diacetyl oxide stir, and oil bath is heated to 80 ℃.The initial time of record heating, system clarification after 20 minutes.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 20 minutes sampling 10ml surveys its optical value until being 0.Threonine reaches 100% racemization, and the required racemization time is 80min.
Embodiment eight: add the 10.54gL-Xie Ansuan in the there-necked flask of 250ml, 50ml Glacial acetic acid and 18ml diacetyl oxide stir, and oil bath is heated to 90 ℃.The initial time of record heating, system clarification in 12 minutes.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 10 minutes sampling 10ml surveys its optical value until being 0.Xie Ansuan reaches 100% racemization, and the required racemization time is 32min.
Embodiment nine: add 13.16gL-Methionin in the there-necked flask of 250ml, 150ml Glacial acetic acid and 27ml diacetyl oxide stir, and oil bath is heated to 100 ℃.The initial time of record heating, after the system clarification in 5 minutes, the time that the record dissolving is required.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 20 minutes sampling 10ml surveys its optical value until being 0.Methionin reaches 100% racemization, and the required racemization time is 124min.
Embodiment ten: add the 17.73gL-phenylalanine in the there-necked flask of 250ml, 100ml Glacial acetic acid and 18ml diacetyl oxide stir, and oil bath is heated to 60 ℃.The initial time of record heating, system clarification in 10 minutes.Get the 10ml sample, be diluted to 25ml with deionized water and survey its optical value.After this every mistake 10 minutes sampling 10ml surveys its optical value until being 0.Phenylalanine reaches 100% racemization, and the required racemization time is 60min.

Claims (10)

1, amino acid racemization method is dissolved in L-amino acid in the organic acid solvent, adds organic acid anhydride, and acidylate takes place in heating, generates the amido-carboxylic acid of racemization; Handle generation DL amino acid through the deacylated tRNA base
(R-CHCOOH)。
NH 3
2, amino acid racemization method according to claim 1 is characterized in that organic acid solvent is a Glacial acetic acid, and organic acid anhydride is a diacetyl oxide.
3, amino acid racemization method according to claim 1 and 2, the mole (mol) that it is characterized in that amino acid and diacetyl oxide is than being 1: 1~1: 3.
4, amino acid racemization method according to claim 1 is characterized in that the organic acid solvent consumption is a 5-10ml/g amino acid.
5, amino acid racemization method according to claim 1, it is characterized in that heating the acidylate temperature is 60~110 ℃.
6, amino acid racemization method according to claim 1 is characterized in that with the amino acid of diacetyl oxide and the racemization of amino acid acidylate L-tyrosine, L-proline(Pro), L-Threonine, L-Xie Ansuan, L-halfcystine, L-phenylalanine, L-Isoleucine being arranged.
7, amino acid racemization method according to claim 1 is characterized in that adding 20 gram L-tyrosine and 22ml diacetyl oxides in the 100ml Glacial acetic acid, is heated with stirring to 110 ℃, and the 100% racemization time of casein amino acid is 30 minutes.
8, amino acid racemization method according to claim 1; it is characterized in that the N-Acetyl tyrosine underpressure distillation after the racemization except that desolvating; add the 3N hydrochloric acid soln; 2 hours hydrolysis ethanoyl reflux; be neutralized to the pH value with sodium hydroxide solution again and be about 3; add activated carbon decolorizing, filtered liquid dropping sodium solution refilters the dry DL-tyrosine that gets to DL tyrosine iso-electric point PH5~6.
9, amino acid racemization method according to claim 1 is characterized in that adding 16.07 gram L-Threonine and 40ml diacetyl oxides in the 75ml Glacial acetic acid, is heated with stirring to 80 ℃, and the 100% racemization time of Threonine is 80 minutes
10, amino acid racemization method according to claim 1 is characterized in that adding 13.16 L-Methionin and the 27ml diacetyl oxides that restrain in the 150ml Glacial acetic acid, is heated with stirring to 100 ℃, and the 100% racemization time of Methionin is 124 minutes.
CN 200410018050 2004-04-29 2004-04-29 Amino acid racemization method Expired - Fee Related CN1228311C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200410018050 CN1228311C (en) 2004-04-29 2004-04-29 Amino acid racemization method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200410018050 CN1228311C (en) 2004-04-29 2004-04-29 Amino acid racemization method

Publications (2)

Publication Number Publication Date
CN1569815A true CN1569815A (en) 2005-01-26
CN1228311C CN1228311C (en) 2005-11-23

Family

ID=34479325

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200410018050 Expired - Fee Related CN1228311C (en) 2004-04-29 2004-04-29 Amino acid racemization method

Country Status (1)

Country Link
CN (1) CN1228311C (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101289410B (en) * 2008-06-06 2011-03-16 山东奥克特化工有限公司 Method for preparing D-phenylalanine
CN101560132B (en) * 2009-05-14 2011-12-14 浙江普洛医药科技有限公司 Method for racemizing chiral amino acid or derivatives of chiral amino acid
CN101575624B (en) * 2009-06-03 2012-07-18 淮北新旗氨基酸有限公司 Microbial enzymes racemization preparation method of DL-alanine
CN103664679A (en) * 2013-12-16 2014-03-26 天津天成制药有限公司 Synthetic method of N-acetyl-beta-alanine nitrate
CN104592083A (en) * 2015-01-06 2015-05-06 宁波海硕生物科技有限公司 Method for preparing N-acetyl-DL-thioproline
CN105063117A (en) * 2015-07-21 2015-11-18 成都百事兴科技实业有限公司 Preparation method of D-arginine monohydrochloride
CN109456220A (en) * 2018-11-16 2019-03-12 浙江工业大学 A kind of racemization method of chirality N- phenylacetylamino acid and its derivative
CN111836800A (en) * 2020-06-18 2020-10-27 苏州园方生物科技有限公司 Preparation method of DL-proline

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101289410B (en) * 2008-06-06 2011-03-16 山东奥克特化工有限公司 Method for preparing D-phenylalanine
CN101560132B (en) * 2009-05-14 2011-12-14 浙江普洛医药科技有限公司 Method for racemizing chiral amino acid or derivatives of chiral amino acid
CN101575624B (en) * 2009-06-03 2012-07-18 淮北新旗氨基酸有限公司 Microbial enzymes racemization preparation method of DL-alanine
CN103664679A (en) * 2013-12-16 2014-03-26 天津天成制药有限公司 Synthetic method of N-acetyl-beta-alanine nitrate
CN104592083A (en) * 2015-01-06 2015-05-06 宁波海硕生物科技有限公司 Method for preparing N-acetyl-DL-thioproline
CN105063117A (en) * 2015-07-21 2015-11-18 成都百事兴科技实业有限公司 Preparation method of D-arginine monohydrochloride
CN105063117B (en) * 2015-07-21 2018-08-17 成都百事兴科技实业有限公司 A kind of preparation method of D-Arg hydrochloride
CN109456220A (en) * 2018-11-16 2019-03-12 浙江工业大学 A kind of racemization method of chirality N- phenylacetylamino acid and its derivative
CN109456220B (en) * 2018-11-16 2021-10-08 浙江工业大学 Racemization method of chiral N-phenylacetyl amino acid and derivative thereof
CN111836800A (en) * 2020-06-18 2020-10-27 苏州园方生物科技有限公司 Preparation method of DL-proline
CN111836800B (en) * 2020-06-18 2021-11-05 苏州园方生物科技有限公司 Preparation method of DL-proline
WO2021253306A1 (en) * 2020-06-18 2021-12-23 苏州园方生物科技有限公司 Method for preparing dl-proline

Also Published As

Publication number Publication date
CN1228311C (en) 2005-11-23

Similar Documents

Publication Publication Date Title
CN1228311C (en) Amino acid racemization method
EP0610048A2 (en) Process for producing optically active alpha-hydrocarboxylic acid having phenyl group
WO2011078172A1 (en) Process for production of optically active 3-substituted glutaric acid monoamide
IE920866A1 (en) Stereoselective enrichment of¹2-amino-3 - hydroxy-3-phenylpropionic acids
AU662998B2 (en) Enzymatic resolution of a racemic mixture of stereospecific gaba-T inhibitors
JP2001328970A (en) Method for producing optically active alpha-amino acid and optically active alpha-amino acid amide
JP2696127B2 (en) Method for producing optically active 2-hydroxycarboxylic acid
JPH10286098A (en) Production of d-amino acid, and production of amine
CN1900298A (en) Method for preparing D-tyrosine by enzyme method
CN1900053A (en) Process for preparing D-alpha-amino isovaleric acid
JP3006615B2 (en) Method for producing D-β-hydroxy amino acid
JP2883712B2 (en) Production method of optically active 1,3-butanediol
JP2005520552A (en) Process for producing optically active β-aminocarboxylic acid from racemic N-acylated β-aminocarboxylic acid
JPH04222591A (en) Production of s-(+)-mandelamide and derivative thereof
JPH0667320B2 (en) Method for producing D-pantolactone
CN1235871C (en) Process for preparing D-tyrosine
CN1164749C (en) Cattle enteropeptidase catalyzing subunit gene and its gene engineering production process
JP5307721B2 (en) (S) -β-Phenylalanine Production Method
JP2786500B2 (en) Production method of optically active 1,3-butanediol
CN103102260B (en) Novel technology for synthesizing S-mandelic acid
JP3647065B2 (en) Method for producing optically active alanine
JP2864277B2 (en) Method for producing optically active amino acids
CN1709861A (en) Method for preparing L-glutamic acid
JPS62294096A (en) Optical resolution of dl-pantolactone
CA2410438A1 (en) Method for optically resolving a racemic alpha-substituted heterocyclic carboxylic acid using enzyme

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee