CN103243032A - Sake candida and fermentation method thereof - Google Patents

Sake candida and fermentation method thereof Download PDF

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CN103243032A
CN103243032A CN2012100302784A CN201210030278A CN103243032A CN 103243032 A CN103243032 A CN 103243032A CN 2012100302784 A CN2012100302784 A CN 2012100302784A CN 201210030278 A CN201210030278 A CN 201210030278A CN 103243032 A CN103243032 A CN 103243032A
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acid
candida
candida sake
substratum
sake
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CN103243032B (en
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刘驰
廖锦绣
汪江林
秦海斌
李乃强
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Kaisai Wusu Biotechnology Co ltd
Cathay R&D Center Co Ltd
CIBT America Inc
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SHANDONG CATHAY BIOTECHNOLOGICAL MATERIAL CO Ltd
Shanghai Cathay Industrial Biotech Ltd
Shanghai Cathay Biotechnology Research and Development Center Co Ltd
Cathay Industrial Biotech Ltd
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Abstract

The invention relates to a novel sake candida bacterial strain and a method for production of long chain diacid by fermentation of the novel sake candida bacterial strain.

Description

Candida sake and fermentation process thereof
Invention field
The present invention relates to the method for candida sake (Candida sake) and fermentative production long-chain biatomic acid thereof.
Background technology
Long-chain biatomic acid (LCDA is also referred to as long chain dicarboxylic acid and long chain diacid) comprises chemical formula HOOC (CH2) nThe diprotic acid of COOH, wherein n 〉=7.LCDA is the base monomer raw material of a series of extraordinary synthetic materialss.Long-chain biatomic acid and derivative monomer thereof can be the important source material of synthetic perfume, engineering plastics, cold resistant plasticizer, senior lubricant and products such as polyamide hot, powder coating for the production of extraordinary nylon, polycarbonate, powder coating, spices, hot melt adhesive, extraordinary lubricant etc.
There is the chemical synthesis process of multiple long-chain biatomic acid in this area, is the mixture of long-chain biatomic acid and short chain diprotic acid but using method is not easy and major part obtains.Need be further purified step when therefore, producing long-chain biatomic acid with these methods.Well known microbial transformation alkane, lipid acid or its ester of utilizing produced long-chain biatomic acid.Because the restriction of existing biological method, chemosynthesis remain the optimization approach of producing long-chain biatomic acid.
This area is general uses several yeast strains to carry out the fermentative production long-chain biatomic acid, and when using alkane or lipid acid to cultivate as carbon source, long-chain biatomic acid produces as by product.Yeast has three Biochemical processes when alkane and lipid acid are carried out metabolism: alkane is to the alpha-oxidation of lipid acid, and lipid acid is to alpha-, and the omega oxidation of omega-dicarboxylic acid and lipid acid are to CO 2Degraded type beta-oxidation with water.With respect to abiotic method for transformation, the bioconversion method of producing diprotic acid has multiple potential advantages.Wherein mainly be to use reproducible raw material as parent material and produce the ability that does not produce harmful chemical by-product in the diprotic acid process.Use another considerable advantage of biological method to be that this method can easily regulate to utilize identical biological catalyst and identical device to produce multiple diprotic acid.Because existing organic chemical synthesis only is suitable for manufacture order kind diprotic acid, the synthetic exploitation that will need the new synthetic schemes of each diprotic acid of several different diprotic acid.On the other hand, the yeast bio catalyzer can utilize identical device, substratum and step to produce the diprotic acid of all lengths, and difference only is to provide the substrate of different carbon atom length to yeast.
Though can utilize various technology to improve for example output of candida tropicalis (Candida tropicalis) fermentation diprotic acid of existing yeast, but can also comprise dodecanedioic acid, undecane dicarboxylic acid, tetradecane diacid, pentadecane diacid and Thapsic acid by providing new candida bacterial strain to produce the long-chain biatomic acid of higher output yield.Therefore an object of the present invention is to provide new bacterial strain and utilize these bacterial strains to produce the method for one or more long-chain biatomic acids.Use this candiyeast to produce long-chain biatomic acid substituted chemistry synthesis method fully, and have the output height, less energy-consumption, the advantage that saves material.
Summary of the invention
In one embodiment of the invention, provide candida sake CAT H4012CCTCC M2011485.Described bacterial classification is preserved in Chinese typical culture collection center (Chinese Wuhan Wuhan University) on December 29th, 2011, and deposit number is: CCTCC M 2011485.
In another embodiment of the present invention, the method of utilizing described candida sake CATH4012CCTCC M 2011485 to produce diprotic acid is provided, and said method comprising the steps of: a. cultivates candida sake CATH4012 in the substratum that contains at least a nitrogenous source and at least a organic substrates; Reclaim the diprotic acid of cultivating the step from a with b..
In yet another embodiment of the invention, the method of utilizing described candida sake CATH4012CCTCC M 2011485 to produce diprotic acid is provided, said method comprising the steps of: a. cultivates candida sake CATH4012 in the substratum that contains at least a nitrogenous source and at least a organic substrates, and wherein said at least a organic substrates is selected from alkane with 12 to 16 carbon atoms or the normal alkane of 12 to 16 carbon atoms; Reclaim the diprotic acid of cultivating the step from a with b..
In the above-described embodiment, described diprotic acid at least a or positive 12 carbon that are 12 carbon to the 16-dicarboxylic acid are at least a to the 16-dicarboxylic acid.
In yet another embodiment of the invention, the method of utilizing described candida sake CATH4012CCTCC M 2011485 to produce diprotic acid is provided, and said method comprising the steps of: a. cultivates candida sake CAT H4012 in the substratum that contains at least a nitrogenous source and n-dodecane hydrocarbon; Reclaim the n-dodecane diacid of cultivating the step from a with b..
In the above-described embodiment, those skilled in the art know operable nitrogenous source.Can use various organonitrogens and inorganic nitrogen.Organic nitrogen source includes but not limited to yeast extract paste, corn steep liquor, extractum carnis, soybean meal hydrolysate, peptone, urea, each seed amino acid and peptide etc., and preferred nitrogenous source is urea.Inorganic nitrogen-sourced nitrate, ammoniacal liquor, liquefied ammonia, ammonium salt, the nitrite etc. of including but not limited to.
The purposes of candida sake H4012CCTCC M 2011485, it is mainly for the production of the application of long-chain biatomic acid.
Description of drawings
Figure 1 shows that the protein sequence comparison diagram of the POX5 gene of CAT H4012.
Figure 2 shows that the POX5 gene DNA sequence comparison diagram of CAT H4012.
Figure 3 shows that the protein sequence comparison diagram of the POX4 gene of CAT H4012.
Figure 4 shows that the POX4 gene DNA sequence comparison diagram of CAT H4012.
Figure 5 shows that the protein sequence comparison diagram of the CYTb5 gene of CAT H4012.
Figure 6 shows that the CYTb5 gene DNA sequence comparison diagram of CAT H4012.
Figure 7 shows that the protein sequence comparison diagram of the CYP52D2 gene of CAT H4012.
Figure 8 shows that the CYP52D2 gene DNA sequence comparison diagram of CAT H4012.
Figure 9 shows that the protein sequence comparison diagram of the CYP52A12 gene of CAT H4012.
Figure 10 shows that the CYP52A12 gene DNA sequence comparison diagram of CAT H4012.
Specific embodiments
By reading following detailed description, those skilled in the art will be more readily understood these and other embodiment of the present invention, key element and advantage.Should be understood that provides following examples with proof and further explains preferred embodiment more of the present invention and aspect, should not be interpreted as limiting its scope.
Although describe similar or suitable method to this paper and material can be used for practice of the present disclosure or test, this paper has described suitable method and material.Unless otherwise defined, all technology used herein are identical with the implication of disclosure one of ordinary skill in the art common sense with scientific terminology.If conflict is arranged, be as the criterion with the definition of this explanation.
When quantity, concentration or other value or parameter provide with scope or height value list, be interpreted as specific arbitrary all scopes that any high low range boundary is formed that disclose, no matter whether scope discloses separately.When this paper enumerates the scope of numerical value, unless otherwise indicated, this scope is intended to comprise its end points, and all integers and mark in this scope.When the range of definition, unintentionally scope of the present invention is limited to the particular value of enumerating.
When being used for this paper, term " comprises ", " comprising ", " having " or its any other variant, is intended to relate to non-exclusive comprising.For example, comprise technology, method, object or the device of a series of key elements and unnecessarily be limited to only those key elements, but can comprise do not list especially or this type of technology, method, object or install other intrinsic key element.
When " one " or " a kind of " be used for to describe multiple key element and composition herein only for convenient and general sense of the present disclosure is provided.This description is understood to include one or at least one and odd number also comprises plural number, unless obviously it is intended to other.
The material of this paper, method and example be usefulness for illustrative purposes only, unless stated otherwise, is not intended to as restriction.
Embodiment
This paper is, and the part term definition is as follows:
Activation medium
Employing is called a kind of aqueous solution substratum of " YPD substratum ", and it comprises following composition: 20g/L glucose, 10g/L yeast extract and 20g/L peptone.Described " YPD substratum " contains the agar of substratum weight 2%, makes substratum gel at room temperature.Described YPD substratum prepares pH regulator to 7.0-7.5 by water and 1N sodium hydroxide solution.With this substratum sterilization 20min under 121 ℃.
The shake-flask seed substratum
Another substratum that is suitable for cultivating bacterial strain of the present invention is " seed culture medium ", and it is a kind of aqueous solution substratum, comprises following composition: 10-30g/L sucrose, 1.5-10g/L corn slurries, 1-10g/L yeast extract, 4-12g/L KH 2PO 4, the heavy wax of 0.5-5g/L urea and 0-50ml/L.Described substratum water preparation, and at 121 ℃ of 20min that sterilize down.Urea is sterilized separately, sterilizes 15 minutes down for 110 ℃, and mix with other compositions of the bacterium of going out the cooling back, uses as seed culture medium.
The shake flask fermentation substratum
Another substratum that is suitable for cultivating bacterial strain of the present invention is " fermention medium ", and it is a kind of aqueous solution substratum, comprises following composition: 1-10g/L corn slurries, 1-10g/L yeast extract, 5-12g/LKH 2PO 4, 0-3g/L sodium-chlor, 4-12g/L saltpetre, 10-40g/L sucrose, the single alkane of 0.5-3g/L urea and 200-300mL/L or mixed alkanes, 0-1g/L vinylformic acid, 0-0.5g/L tween 80.Described by water and 1N sodium hydroxide solution with pH regulator to 7.5-7.8.With this substratum sterilization 20min under 121 ℃.Urea is sterilized separately, sterilizes 15 minutes down for 110 ℃, and mix with other compositions of the bacterium of going out the cooling back, uses as fermention medium.
According to the present invention, bacterial strain can be used in the various zymotechniques, comprises 500ml fermentation shake flask technology, and it comprises as follows:
With transfering loop uniform spreading on the YPD substratum of the sterilization of cell in the test tube slant is opened.This inclined-plane was cultivated 2 days under stabilizing to 29-30 ℃.Then 1/3rd inoculations of this slant culture are contained in 500ml and shake in the sterilization seed culture medium of the 30ml in the bottle and be 29-30 ℃ in temperature and cultivated 36-48 hour down, bottle speed of shaking is 200-250rpm, and the amplitude of shaking is 2.5-3.5cm.Meat soup with seed fermentation is seeded to the fermention medium that is contained in the sterilization in the 500ml fermentation flask then.This culture is 29-30 ℃ in temperature to be cultivated 90-120 hour down, and bottle speed of shaking is 200-240rpm, and the amplitude of shaking is 2.5-3.5cm, and by monitoring with the adjusting of 1N sodium hydroxide solution pH is maintained between the 7.0-8.0.Dicarboxylic acid concentration in this fermenting broth can be measured after this step.
The evaluation of embodiment 1 candida sake
Screen candida sake (Candida sake) from the oil field, handled the bacterial strain that obtains the positive SL-AH of high yield through chemomorphosis.
The evaluation of candida sake (Candida sake):
1. sample collecting: Accessories during Binzhou suburb, Shandong Province Shengli Oil Field is gathered, and is chocolate crude oil pollution soil sample.
2. the strain separating of collect specimen: it is 10 that all soil samples that will collect are made extent of dilution respectively -3, 10 -4, 10 -5, 10 -6Diluent be coated with at the YPD flat board respectively.Culture condition: 30 ℃, 48 hours.
Cultivate through separating for several times, obtain oil field saccharomycetic purifying list bacterium colony.
3. identify
With " saccharomycetic means of taxonomic research " (The Yeasts:A Taxonomic Study) the 90th chapter mycocandida (Candida Berkhout) 90.241 candida sakes (Candida sake) comparisons (P1209), determine it is candida sake.
3.1 the utilization of carbon source and nitrogenous source
Under known microorganism identification, carry out nutrition utilization experiment.Add following nitrogenous source or carbon source in defined medium, whether yeast culture is grown to Rule of judgment after 2 days or 3 days, judges negative and the positive, and the result is as follows:
Figure BSA00000668720300061
Figure BSA00000668720300071
Other test: be that carbon source, nitrogenous source are (+) with the N-acetyl-glucosamine
Be (-) down at 37 ℃
Urase is (-)
Identifying this bacterial strain with this is candida sake (Candida sake).
Embodiment 2 candida sake CAT H4012 mutagenesis screening steps
1. a strain is separated the candida sake obtain, it is stand-by to make the preservation of glycerine pipe.
2. get stand-by one of the glycerine pipe bacterial strain that is preserved in cryogenic refrigerator and put room temperature and thaw, the back that thaws is inserted and is equipped with in the 500ml triangular flask of 50mlYPD substratum, cultivates 20-24h in the rotary shaker that 29 ℃ of rotating speeds are 210rpm.
3. add the YPD nutrient solution of above-mentioned 10ml in the aseptic centrifuge tube of 15ml, centrifugal 2 minutes of 2000rpm removes supernatant liquor, the physiological saline centrifuge washing with 0.85% 3 times.
4. remove supernatant liquor, add 2.5% aseptic lithium chloride 10ml, the preparation bacteria suspension.
5. the NTG mutagenic compound that take by weighing 0.08mg add in the aseptic centrifuge tube of 15ml, and add the physiological saline of 10ml 0.85%, mixing.
6. each the 10ml liquid in 3 and 4 is added in the aseptic plate that is placed with the 15mm*3mm stirrer of 90mm, build loam cake.
7. above-mentioned flat board is by handling 2 of refabrication with quadrat method
8. this plate is put on the magnetic stirring apparatus respectively stir process 10,15,20 minutes.
9. each handles dull and stereotyped processing by the following method respectively.
10. above-mentioned treatment solution is got in the aseptic centrifuge tube of 10ml adding 15ml, and centrifugal 2 minutes of 2000rpm removes supernatant liquor, the physiological saline centrifuge washing with 0.85% 3 times.
11. remove supernatant liquor, the physiological saline with 0.85% carries out gradient dilution step by step.
12. drawing 0.15ml bacterium liquid, every extent of dilution carries out the flat board coating.
13. putting 29 ℃ of incubators, the flat board after the coating is inverted cultivation 3-4 days.
14. picking is cultivated ripe single bacterium and is transferred into the 15*150mm test tube slant, puts 29 ℃ of incubators and cultivates 2 days.
Be equipped with in the 250ml triangular flask of 10ml fermention medium 15. get 1/3rd inclined-plane thalline accesses after the slant culture maturation, in the rotary shaker that 29 ℃ of rotating speeds are 210rpm, cultivated 4 days.4 ℃ of refrigerator cold-storages are put on the residue inclined-plane.
16. calculate the alkali consumption that shakes bottle average alkali consumption and screening bacterial strain of control strain, definite consumption buck that will screen bacterial strain is put down, and generally improves more than 10% than primary dcreening operation control strain alkali consumption.
17. the bacterial strain of how much determining to carry out answering again sieve according to the fermentation shake flask alkali consumption.
18. general 100 strains are shaken and are chosen the high bacterial strain of 5 strain alkali consumptions in bottle primary dcreening operation bacterial strain and carry out multiple sieve.
19. choose the primary dcreening operation inclined-plane of multiple sieve bacterial strain correspondence, above-mentionedly connect remaining 2/3rds inclined-planes behind the primary dcreening operation, shovel is got 1/5th inclined-plane thalline switching inclined-plane F2 again, puts 29 ℃ of incubators and cultivates 2 days.The residue inclined-plane continues to put refrigerator cold-storage.
Be equipped with in the 500ml triangular flask of 30ml seed culture medium 20. cultivate whole whole access of ripe inclined-plane thalline, in the rotary shaker that 29 ℃ of rotating speeds are 210rpm, cultivate 44-48h.Simultaneously 1 glycerine pipe bacterium liquid of control strain also all being inserted 1 seed shakes in the bottle.
Be equipped with in the 500ml triangular flask of 15ml fermention medium 21. the seed liquor after the cultivation maturation is drawn the 3ml adding, in the rotary shaker that 29 ℃ of rotating speeds are 210rpm, cultivate 110h and put bottle mensuration.General each seed bottle correspondence connects 2 bottles of fermented liquids.
22. multiple sieve shakes a bottle measuring method: acid base titration
23. through repeatedly screening the bacterial strain that obtains the high yield SL-AH, called after CAT H4012.
According to candida tropicalis diprotic acid pathways metabolism, selected 15 genes relevant with producing diprotic acid, specific as follows: CYP52A12, CYP52A13, CYP52A14, CYP52A15, CYP52A16, CYP52A17, CYP52A18, CYP52A19, CYP52A20, CYP52D2, POX4, POX5, CPR A, CPR B, and CYTb5.Candida sake CAT H4012 is delivered to specialty order-checking mechanism, adopt Illumina platform end pairing sequencing to carry out genome sequencing, and from genome sequence, extract the gene order with these 15 candida tropicalis dna homologs.Find that candida sake CAT H4012CCTCC M of the present invention 2011485 has any different at the homologous gene of following gene and candida tropicalis: CYP52A12, CYP52D2, POX4, POX5 and CYTb5.Fig. 1-Figure 10 is seen in the gene order contrast.
Embodiment 3 n-dodecane hydrocarbon fermentations
Diprotic acid testing method in the fermented product:
The preparation of diprotic acid sample: fermentation ends, in the 500mL triangular flask, with 6mol/L hydrochloric acid soln adjust pH to 3.0, every bottle adds the 120mL ether, shakes 100 times, place more than the 30min, standing demix takes out the 40mL ether extracted liquid, is added in the 100mL beaker, remove ether, obtain white solid.Carry out the mensuration of diprotic acid then.
Determine the length of diprotic acid, or monoprotic acid do not arranged, then need by vapor-phase chromatography GC that after soon product is handled, separate through capillary column, the diprotic acid of different carbon chain lengths and monoprotic acid go out the peak at different time, therefore just can determine final product.For example: chromatographic apparatus model (GC9800): capillary column FFAP 30*0.53mm*0.5um, detector FID determines that final product compares with retention time Rf and standard substance to draw, standard substance are the AR reagent that Sigma or TGI company produce.
The mensuration of diprotic acid output: the white solid that extraction is obtained, add 100mL inner mark solution (tetramethyl ammonium hydroxide solution that contains the 4mg/mL hexanodioic acid), after the whole dissolvings of the white solid that extraction obtains, air inlet phase chromatogram, the area ratio of mark and sample in the record; Take by weighing standard substance (the diprotic acid standard substance of different carbon chain lengths simultaneously, available from Sigma or TGI reagent company) about 0.4000g, add 100mL inner mark solution (tetramethyl ammonium hydroxide solution that contains the 4mg/mL hexanodioic acid), after standard substance all dissolve, air inlet phase chromatogram, the area ratio of record standard product and sample; Calculate and the calculating of area ratio according to the area normalization method in the vapor-phase chromatography, can obtain the diprotic acid content of different carbon chain lengths.Obtain the standard substance of known quality and the area ratio of internal standard substance by vapor-phase chromatography, so obtain area than with the relation of mass ratio.Obtain the area ratio of sample and internal standard substance again by vapor-phase chromatography, according to aforementioned area than and the relation of mass ratio and the quality of internal standard substance, obtain the quality of sample.
The technical process of 500ml shake flask fermentation and description:
Inclined-plane seed culture-shake-flask seed cultivation-shake flask fermentation
The inclined-plane seed culture: the switching inclined-plane, freeze-drying pipe inclined-plane of 4 ℃ of refrigerator preservations, the seed of transferring behind the cultivation 48h in 29 ℃ of incubators shakes bottle, and seed culture is between 29 ℃ of shaking tables, and 230rpm cultivates secondary fermentation in 48 hours.Fermentation shake flask inserts the seed of 3.0mL, after the inoculation, shakes bottle and puts between 29 ℃ of shaking tables, puts bottle behind the 230rpm shaking culture 90-110h and measures the acid amount of producing.
The substratum that uses in the present embodiment is specific as follows:
The inclined-plane seed culture medium:
20g/L glucose, 10g/L yeast extract and 20g/L peptone, and be 2% agar of YPD substratum weight.Add the agar purpose and be to make substratum gel at room temperature.
The shake-flask seed substratum is as follows:
Title Proportioning
Sucrose 20g/L
Corn steep liquor 3g/L
Yeast extract paste 5g/L
KH 2PO 4 8g/L
Heavy wax 50ml/L
Urea (sterilization separately) 3g/L
Take by weighing various starting material and record the amount that takes by weighing according to seed culture medium proportioning table, taking by weighing the back that finishes dissolves fully with the tap water starting material, the quantitative charger packing, 30mL/ 500mL shakes bottle, packing, after the packing with the 1.0mL liquid-transfering gun toward shaking the heavy wax that bottle adds 1.5ml, 6 layers of gauze and kraft paper are wrapped up back 121 ℃ of 20min that sterilize down, and is standby.
Fermention medium:
Figure BSA00000668720300101
Figure BSA00000668720300111
Take by weighing various starting material and record the amount that takes by weighing according to the fermention medium proportioning, taking by weighing the back that finishes dissolves starting material with tap water fully, regulate pH to 7.5 with alkali lye, 15mL/ 500mL shakes bottle, add the n-dodecane hydrocarbon in the fermention medium, wrap up back 121 ℃ of 20min that sterilize down with 6 layers of gauze and kraft paper, standby.
500ml shake flask fermentation result:
Single alkane 500ml shake flask fermentation result:
Bacterial strain The diprotic acid kind Produce acid amount g/L
CAT H4012 Positive 12 carbon 93.75
The fermentation of embodiment 4 mixed alkanes
Mixed alkanes is that n-dodecane hydrocarbon, n-tridecane hydrocarbon, n-tetradecane hydrocarbon, Pentadecane hydrocarbon and n-hexadecane hydrocarbon (nC12+nC13+nC14+nC15+nC16) equal-volume mix.Fermention medium is as follows:
Figure BSA00000668720300112
Figure BSA00000668720300121
Fermenting process, the diprotic acid kind is all identical with embodiment 3 with the output test in the fermented product.
Mixed alkanes 500ml shake flask fermentation result:
Figure BSA00000668720300122
Figure ISA00000668688700011
Figure ISA00000668688700031
Figure ISA00000668688700041
Figure ISA00000668688700061
Figure ISA00000668688700071
Figure ISA00000668688700081
Figure ISA00000668688700111
Figure ISA00000668688700121
Figure ISA00000668688700131
Figure ISA00000668688700141

Claims (10)

1. candida sake (Candida sake) CAT H4012 preserving number is CCTCC M2011485.
2. prepare the method for diprotic acid, said method comprising the steps of: a. cultivates candida sake CAT H4012 in the substratum that contains at least a nitrogenous source and at least a organic substrates; Reclaim the diprotic acid of cultivating the step from a with b..
3. method as claimed in claim 2, wherein said at least a organic substrates is selected from the alkane with 12 to 16 carbon atoms.
4. method as claimed in claim 2, wherein said at least a organic substrates is selected from the normal alkane with 12 to 16 carbon atoms.
5. method as claimed in claim 2, wherein said at least a organic substrates is the n-dodecane hydrocarbon.
6. method as claimed in claim 2, wherein said diprotic acid at least a or positive 12 carbon that are 12 carbon to the 16-dicarboxylic acid are at least a to the 16-dicarboxylic acid.
7. as each described method among the claim 2-6, wherein said nitrogenous source is organic nitrogen source or inorganic nitrogen-sourced.
8. method as claimed in claim 7, wherein said organic nitrogen source is one or more in yeast extract paste, corn steep liquor, extractum carnis, soybean meal hydrolysate, peptone, urea, each seed amino acid and the peptide.
9. method as claimed in claim 7, wherein said inorganic nitrogen-sourced be in nitrate, ammoniacal liquor, liquefied ammonia, ammonium salt, the nitrite one or more.
10. candida sake is being produced the application of long-chain biatomic acid according to claim 1.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3550014A1 (en) * 2018-04-04 2019-10-09 Shanghai Cathay Biotech R&D Center Ltd. Directed evolution of cyp52a12 gene and its use in dicarboxylic acid production
CN110343675A (en) * 2018-04-04 2019-10-18 上海凯赛生物技术研发中心有限公司 The directed evolution of CYP52A12 gene and its application in binary acid production
CN110684784A (en) * 2018-07-06 2020-01-14 上海凯赛生物技术股份有限公司 Long-chain dibasic acid with low content of monobasic acid impurities and production method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1233658A (en) * 1999-05-28 1999-11-03 清华大学 Method for screening candida for high prodn. of long chain diacid
CN1570124A (en) * 2004-05-12 2005-01-26 上海凯赛生物技术研发中心有限公司 Long chain normal dibasic acid production method
CN101225411A (en) * 2007-11-30 2008-07-23 中国科学院微生物研究所 New method for biosynthetic production of mixed long-chain dibasic acid
CN102191187A (en) * 2011-04-01 2011-09-21 山东华星环保集团有限公司 Candida lipolytica strain and method for preparing long chain dicarboxylic acid by using candida lipolytica strain

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1233658A (en) * 1999-05-28 1999-11-03 清华大学 Method for screening candida for high prodn. of long chain diacid
CN1570124A (en) * 2004-05-12 2005-01-26 上海凯赛生物技术研发中心有限公司 Long chain normal dibasic acid production method
CN101225411A (en) * 2007-11-30 2008-07-23 中国科学院微生物研究所 New method for biosynthetic production of mixed long-chain dibasic acid
CN102191187A (en) * 2011-04-01 2011-09-21 山东华星环保集团有限公司 Candida lipolytica strain and method for preparing long chain dicarboxylic acid by using candida lipolytica strain

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3550014A1 (en) * 2018-04-04 2019-10-09 Shanghai Cathay Biotech R&D Center Ltd. Directed evolution of cyp52a12 gene and its use in dicarboxylic acid production
CN110343675A (en) * 2018-04-04 2019-10-18 上海凯赛生物技术研发中心有限公司 The directed evolution of CYP52A12 gene and its application in binary acid production
US11091742B2 (en) 2018-04-04 2021-08-17 Cathay Biotech Inc. Directed evolution of CYP52A12 gene and its use in dicarboxylic acid production
CN110343675B (en) * 2018-04-04 2023-05-12 上海凯赛生物技术股份有限公司 Directed evolution of CYP52A12 gene and application thereof in dibasic acid production
US11753629B2 (en) 2018-04-04 2023-09-12 Cathay Biotech Inc. Directed evolution of CYP52A12 gene and its use in dicarboxylic acid production
CN110684784A (en) * 2018-07-06 2020-01-14 上海凯赛生物技术股份有限公司 Long-chain dibasic acid with low content of monobasic acid impurities and production method thereof
CN110684784B (en) * 2018-07-06 2023-08-08 上海凯赛生物技术股份有限公司 Long-chain dibasic acid with low content of monobasic acid impurity and production method thereof

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