CN102605015A - L-alanine production method - Google Patents
L-alanine production method Download PDFInfo
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- CN102605015A CN102605015A CN201110025960XA CN201110025960A CN102605015A CN 102605015 A CN102605015 A CN 102605015A CN 201110025960X A CN201110025960X A CN 201110025960XA CN 201110025960 A CN201110025960 A CN 201110025960A CN 102605015 A CN102605015 A CN 102605015A
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Abstract
The invention discloses an L-alanine production method comprising the following steps: activating passage pseudomonas dacunhae on a sterile agarslantculture-medium; inoculating and culturing the activated pseudomonas dacunhae in a sterile shake-flask seed liquid medium; when the net gain of OD ranges from 0.5 to 0.6, and the pH value ranges from 8.0 to 9.0 and is constant, adding aspartate in a flow way, and controlling the lowest pH value at 6.0; and when the pH value is 6.0 and is constant, finishing fermentation. The shake-flask seed liquid medium comprises 1% of sodium glutamate, 0.8% of peptone, 0.5% of sodium chloride, 0.1% of magnesium sulfate, 0.05% of monopotassium phosphate and 0.55% of corn powder; and the agarslantculture-medium comprises 1% of sodium glutamate, 0.8% of peptone, 0.5% of sodium chloride, 0.1% of magnesium sulfate, 0.05% of monopotassium phosphate, 0.5% of yeast extract, 0.5% of beef extract and 2% of agar. According to the method, the yield and purity of produced L-alanine are high.
Description
Technical field
The present invention relates to a kind of method of the L-of production L-Ala.
Background technology
The L-L-Ala (L-Alanine) also claim α-An Jibingsuan; Be one of amino acid that life entity is interior with carbohydrate metabolism is closely related, demand is more; In industries such as medicine, food and chemical industry, be used widely; And become the another important amino acid industry after L-glutamic acid, Methionin, it is very necessary greatly developing production.Present L-L-Ala working method is for being main raw materials for production with fumaric acid, and whole cell enzyme catalysis biological respinse method is produced the L-L-Ala.
Summary of the invention
The method that the purpose of this invention is to provide a kind of L-of production L-Ala.
The method of production L-L-Ala provided by the present invention comprises the steps:
The activation moral A Kun that goes down to posterity breathes out pseudomonas on aseptic slant medium; Moral A Kun Kazakhstan pseudomonas after the activation is inoculated in the aseptic shake-flask seed liquid culture medium to be cultivated; When OD has a net increase of 0.5~0.6, the pH value be 8.0~9.0 continuous when constant stream add aspartic acid, control pH value is minimum to be 6.0; When the pH value is 6.0, accomplish fermentation when constant continuously;
Said shake-flask seed liquid culture medium is Sodium Glutamate 1%, peptone 0.8%, sodium-chlor 0.5%, sal epsom 0.1%, potassium primary phosphate 0.05%, corn dry powder 0.55%.
Said slant medium is Sodium Glutamate 1%, peptone 0.8%, sodium-chlor 0.5%, sal epsom 0.1%, potassium primary phosphate 0.05%, yeast extract paste 0.5%, Carnis Bovis seu Bubali cream 0.5%, agar 2%.
The method of production L-L-Ala of the present invention, the output of L-L-Ala and purity are high.
Embodiment
Following percentage composition is the quality percentage composition like no specified otherwise.
Embodiment
Shake-flask seed liquid culture medium: Sodium Glutamate 1%, peptone 0.8%, sodium-chlor 0.5%, sal epsom 0.1%, potassium primary phosphate 0.05%, corn dry powder 0.55%.
Slant medium: Sodium Glutamate 1%, peptone 0.8%, sodium-chlor 0.5%, sal epsom 0.1%, potassium primary phosphate 0.05%, yeast extract paste 0.5%, Carnis Bovis seu Bubali cream 0.5%, agar 2%.
The activation moral A Kun that goes down to posterity breathes out pseudomonas on aseptic slant medium; Culture temperature 30 ± ℃, the moral A Kun Kazakhstan pseudomonas after the activation is inoculated in the seeding tank that aseptic shake-flask seed liquid culture medium is housed cultivates 30 ± 1 ℃ of jar temperature; Tank pressure 0.05~0.08MPa, ventilation 20~24m
3/ h, when OD has a net increase of 0.5~0.6, endpoint pH is that 8.0~9.0 continuous 6 hours streams when constant add aspartic acid, control pH value, minimum is 6.0, and when pH value is 6.0, continuous 1 hour is constant, and completion is fermented.
1M
3The seeding tank fermented liquid can transform 2.5 tons of aspartic acids, transformation efficiency 95%, L-L-Ala extraction yield 98%.
Claims (1)
1. a method of producing the L-L-Ala comprises the steps:
The activation moral A Kun that goes down to posterity breathes out pseudomonas on aseptic slant medium; Moral A Kun Kazakhstan pseudomonas after the activation is inoculated in the aseptic shake-flask seed liquid culture medium to be cultivated; When OD has a net increase of 0.5~0.6, the pH value be 8.0~9.0 continuous when constant stream add aspartic acid, control pH value is minimum to be 6.0; When the pH value is 6.0, accomplish fermentation when constant continuously;
Said shake-flask seed liquid culture medium is Sodium Glutamate 1%, peptone 0.8%, sodium-chlor 0.5%, sal epsom 0.1%, potassium primary phosphate 0.05%, corn dry powder 0.55%.
Said slant medium is Sodium Glutamate 1%, peptone 0.8%, sodium-chlor 0.5%, sal epsom 0.1%, potassium primary phosphate 0.05%, yeast extract paste 0.5%, Carnis Bovis seu Bubali cream 0.5%, agar 2%.
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CN201110025960XA CN102605015A (en) | 2011-01-20 | 2011-01-20 | L-alanine production method |
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CN201110025960XA CN102605015A (en) | 2011-01-20 | 2011-01-20 | L-alanine production method |
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CN102605015A true CN102605015A (en) | 2012-07-25 |
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CN201110025960XA Pending CN102605015A (en) | 2011-01-20 | 2011-01-20 | L-alanine production method |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105441500A (en) * | 2015-12-18 | 2016-03-30 | 安徽丰原发酵技术工程研究有限公司 | Fermentation method for L-alanine |
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US3463704A (en) * | 1964-11-09 | 1969-08-26 | Ajinomoto Kk | Method of producing alanine by enzyme action |
JPH02242690A (en) * | 1989-03-16 | 1990-09-27 | Mitsubishi Petrochem Co Ltd | Production of l-alanine |
EP0455170A2 (en) * | 1990-04-27 | 1991-11-06 | Mitsubishi Petrochemical Co., Ltd. | Process for culturing microorganisms of the genus Pseudomonas and process for producing L-alanine using said microorganisms |
JPH0538292A (en) * | 1991-05-30 | 1993-02-19 | Mitsubishi Petrochem Co Ltd | Production of l-alanine |
CN1105068A (en) * | 1994-01-03 | 1995-07-12 | 欧阳平凯 | L-alanine preparing method and its application |
CN1405317A (en) * | 2002-11-07 | 2003-03-26 | 南京工业大学 | D-aminosuccinic acid and L-alanine preparation method |
CN101210230A (en) * | 2006-12-28 | 2008-07-02 | 浙江工业大学 | Gene engineering bacterium for producing beta-alanine and its preparation and application |
CN101575624A (en) * | 2009-06-03 | 2009-11-11 | 淮北新旗氨基酸有限公司 | Microbial enzymes racemization preparation method of DL-alanine |
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-
2011
- 2011-01-20 CN CN201110025960XA patent/CN102605015A/en active Pending
Patent Citations (9)
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US3463704A (en) * | 1964-11-09 | 1969-08-26 | Ajinomoto Kk | Method of producing alanine by enzyme action |
JPH02242690A (en) * | 1989-03-16 | 1990-09-27 | Mitsubishi Petrochem Co Ltd | Production of l-alanine |
EP0455170A2 (en) * | 1990-04-27 | 1991-11-06 | Mitsubishi Petrochemical Co., Ltd. | Process for culturing microorganisms of the genus Pseudomonas and process for producing L-alanine using said microorganisms |
JPH0538292A (en) * | 1991-05-30 | 1993-02-19 | Mitsubishi Petrochem Co Ltd | Production of l-alanine |
CN1105068A (en) * | 1994-01-03 | 1995-07-12 | 欧阳平凯 | L-alanine preparing method and its application |
CN1405317A (en) * | 2002-11-07 | 2003-03-26 | 南京工业大学 | D-aminosuccinic acid and L-alanine preparation method |
CN101210230A (en) * | 2006-12-28 | 2008-07-02 | 浙江工业大学 | Gene engineering bacterium for producing beta-alanine and its preparation and application |
CN101575624A (en) * | 2009-06-03 | 2009-11-11 | 淮北新旗氨基酸有限公司 | Microbial enzymes racemization preparation method of DL-alanine |
CN101580864A (en) * | 2009-06-11 | 2009-11-18 | 安徽华恒生物工程有限公司 | Method for producing optically pure L-alanine by one pseudomonas and two enzymes |
Non-Patent Citations (5)
Title |
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《Chemical Engineering Journal》 19971231 Giizide Calik et al Bioprocess parameters and oxygen transfer effects in the growth of Pseudomonas dacunhae for L-alanine production 第109-116页 1 第65卷, * |
《Enhanced Production of -Aspartate-Decarboxylase by Nitrogen Source in Pseudomonas dacunhae》 20061231 Dong Chung Kim et al Enhanced Production of -Aspartate -Decarboxylase by Nitrogen Source in pseudomonas dacunhae 全文 1 第49卷, 第3期 * |
DONG CHUNG KIM ET AL: "Enhanced Production of -Aspartate -Decarboxylase by Nitrogen Source in pseudomonas dacunhae", 《ENHANCED PRODUCTION OF -ASPARTATE-DECARBOXYLASE BY NITROGEN SOURCE IN PSEUDOMONAS DACUNHAE》 * |
GIIZIDE CALIK ET AL: "Bioprocess parameters and oxygen transfer effects in the growth of Pseudomonas dacunhae for L-alanine production", 《CHEMICAL ENGINEERING JOURNAL》 * |
徐虹等: "利用假单胞菌天冬氨酸-B-脱羧酶高效生产 L-丙氨酸", 《南京化工学院学报》 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105441500A (en) * | 2015-12-18 | 2016-03-30 | 安徽丰原发酵技术工程研究有限公司 | Fermentation method for L-alanine |
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Address after: 265709 Shandong province Longkou City Langao bio chemical industrial park Applicant after: Yantai Hengyuan Bioengineering Co., Ltd. Address before: High Town, Siping Village 265709 Shandong province Longkou City blue Applicant before: Yantai Hengyuan Bioengineering Co., Ltd. |
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Application publication date: 20120725 |