CN111718968B - 一种提高卷枝毛霉wj11中链脂肪酸产量的方法 - Google Patents
一种提高卷枝毛霉wj11中链脂肪酸产量的方法 Download PDFInfo
- Publication number
- CN111718968B CN111718968B CN202010772667.9A CN202010772667A CN111718968B CN 111718968 B CN111718968 B CN 111718968B CN 202010772667 A CN202010772667 A CN 202010772667A CN 111718968 B CN111718968 B CN 111718968B
- Authority
- CN
- China
- Prior art keywords
- medium
- fermentation
- chain fatty
- fatty acid
- mucor
- 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.)
- Expired - Fee Related
Links
- 150000004667 medium chain fatty acids Chemical class 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 8
- 241000306281 Mucor ambiguus Species 0.000 title abstract description 6
- 238000000855 fermentation Methods 0.000 claims abstract description 28
- 230000004151 fermentation Effects 0.000 claims abstract description 28
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims abstract description 5
- 238000011081 inoculation Methods 0.000 claims abstract 4
- 241000235395 Mucor Species 0.000 claims description 16
- 239000002609 medium Substances 0.000 claims description 9
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 6
- 229910021094 Co(NO3)2-6H2O Inorganic materials 0.000 claims description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 3
- NGPGDYLVALNKEG-UHFFFAOYSA-N azanium;azane;2,3,4-trihydroxy-4-oxobutanoate Chemical compound [NH4+].[NH4+].[O-]C(=O)C(O)C(O)C([O-])=O NGPGDYLVALNKEG-UHFFFAOYSA-N 0.000 claims description 3
- 229940041514 candida albicans extract Drugs 0.000 claims description 3
- 239000008103 glucose Substances 0.000 claims description 3
- 239000001963 growth medium Substances 0.000 claims description 3
- 239000012138 yeast extract Substances 0.000 claims description 3
- 238000011218 seed culture Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims 1
- 235000014113 dietary fatty acids Nutrition 0.000 abstract description 6
- 229930195729 fatty acid Natural products 0.000 abstract description 6
- 239000000194 fatty acid Substances 0.000 abstract description 6
- 150000004665 fatty acids Chemical class 0.000 abstract description 6
- 239000000203 mixture Substances 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract description 2
- 230000000813 microbial effect Effects 0.000 abstract description 2
- 230000001737 promoting effect Effects 0.000 abstract description 2
- 239000004519 grease Substances 0.000 abstract 2
- 238000007792 addition Methods 0.000 description 7
- 239000003921 oil Substances 0.000 description 7
- 235000019198 oils Nutrition 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- GHVNFZFCNZKVNT-UHFFFAOYSA-N decanoic acid Chemical compound CCCCCCCCCC(O)=O GHVNFZFCNZKVNT-UHFFFAOYSA-N 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 3
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- VZCCETWTMQHEPK-UHFFFAOYSA-N gamma-Linolensaeure Natural products CCCCCC=CCC=CCC=CCCCCC(O)=O VZCCETWTMQHEPK-UHFFFAOYSA-N 0.000 description 2
- VZCCETWTMQHEPK-QNEBEIHSSA-N gamma-linolenic acid Chemical compound CCCCC\C=C/C\C=C/C\C=C/CCCCC(O)=O VZCCETWTMQHEPK-QNEBEIHSSA-N 0.000 description 2
- 235000020664 gamma-linolenic acid Nutrition 0.000 description 2
- 229960002733 gamolenic acid Drugs 0.000 description 2
- 238000010353 genetic engineering Methods 0.000 description 2
- 239000002054 inoculum Substances 0.000 description 2
- 150000002632 lipids Chemical class 0.000 description 2
- WWZKQHOCKIZLMA-UHFFFAOYSA-N octanoic acid Chemical compound CCCCCCCC(O)=O WWZKQHOCKIZLMA-UHFFFAOYSA-N 0.000 description 2
- 101100283604 Caenorhabditis elegans pigk-1 gene Proteins 0.000 description 1
- 239000005632 Capric acid (CAS 334-48-5) Substances 0.000 description 1
- 239000005635 Caprylic acid (CAS 124-07-2) Substances 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 208000008589 Obesity Diseases 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003240 coconut oil Substances 0.000 description 1
- 235000019864 coconut oil Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 150000004668 long chain fatty acids Chemical class 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000020824 obesity Nutrition 0.000 description 1
- 229960002446 octanoic acid Drugs 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000003346 palm kernel oil Substances 0.000 description 1
- 235000019865 palm kernel oil Nutrition 0.000 description 1
- 210000003240 portal vein Anatomy 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000013587 production medium Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
- C12P7/6409—Fatty acids
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/14—Fungi; Culture media therefor
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/40—Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- Biotechnology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Botany (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mycology (AREA)
- Medicinal Chemistry (AREA)
- Tropical Medicine & Parasitology (AREA)
- Virology (AREA)
- Biomedical Technology (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
本发明是一种促进卷枝毛霉WJ11生产中链脂肪酸的方法,属于微生物油脂领域。本发明利用在发酵培养基中添加氯化钴溶液,改变了卷枝毛霉的油脂组成,使其中链脂肪酸的占比增加,发酵条件为:添加氯化钴的终浓度为2 mmol/L,添加时间为接种后的24 h,接入种子液的接种量为10%,发酵罐转速为700 rpm,pH为6.2,空气流速为1 vvm,发酵温度为28℃,发酵时间为120 h,最终中链脂肪酸的含量从1.31%提高到了15.29%,其产量为1109.74 mg/L。
Description
技术领域
本发明属于微生物油脂领域。该发酵方法能促进卷枝毛霉WJ11产出中链脂肪酸,并且产量可观。
背景技术
丝状真菌在自然界中广泛存在,卷枝毛霉(
Mucor circinelloides)就是其中一种常见的高产油脂的菌种,它能够产生大量的亚油酸、γ-亚麻酸并在细胞内积累。本发明所用的菌种为卷枝毛霉WJ11,它可以产生高达占细胞干重(CDW)36%的脂质,但这些油脂都是C14以上的长链脂肪酸,比如γ-亚麻酸(顺式-6,9,12-十八碳三烯酸)等。
中链脂肪酸 (MCFA) 是一定链长脂肪酸的统称,一般是指辛酸、癸酸等六碳链到十二碳链的脂肪酸。中链脂肪酸是食品、医疗和化工产品的重要前体。摄入的中链脂肪酸通过门静脉直接运输到肝脏参与氧化,从而快速提供能量,不会引起肥胖,非常有利于极限运动员和减肥人群。自然界中的中链脂肪酸主要存在于椰子油、棕榈仁油中,但含量不高(低于总油脂含量的15%)。在工业生产中,中链脂肪酸的来源主要是人工化学合成或者基因工程改造,通过产油微生物来生产中链脂肪酸的方法也较少。
发明内容
本发明展开了一种方便有效的提高中链脂肪酸产量的方法,即向发酵培养基中添加氯化钴溶液。这相对于人工化学合成和基因工程操作省时省力,收益可观。
技术方案:
在之前的实验中,我们选取了Al3+、Fe2+、Co2+、Ni2+、Cu2+等多种金属离子分别添加到卷枝毛霉WJ11的培养基中,测定卷枝毛霉WJ11产生的油脂含量以后发现Co2+的加入使卷枝毛霉WJ11产出了中链脂肪酸C10和C12。对此现象我们又进行了深入的研究,通过控制Co2+的浓度和Co2+的添加时间不同从而确定了最优的发酵条件。
本发明的收益效果:
Co2+的加入能促进卷枝毛霉WJ11中链脂肪酸的合成,使其比例升高,实验选出了最优的发酵条件即在24 h时加入2 mmol/L Co2+,在此发酵条件下Co2+促进卷枝毛霉中链脂肪酸合成的效果最好,能使卷枝毛霉产生占总油脂含量15.3%的中链脂肪酸,其含量达到1109.7 mg/L。
具体实施方式
菌种:
卷枝毛霉WJ11(
Mucor circinelloides WJ11, CCTCC No. M 2014424; ChinaCenter for Type Culture Collection)
最佳Co2+浓度的确定:
本发明设计了6组不同的Co2+浓度梯度,将它们在配制培养基时分别加入6个完全相同的挡板三角瓶中,每个三角瓶中都装有200 mL发酵培养基,配方为葡萄糖 80 g/L,MgSO4·7H2O 1.5 g/L,酒石酸铵2.0 g/L,KH2PO4 7 g/L,Na2HPO4 2 g/L,酵母抽提物 1.5g/L,CaCl2·2H2O 0.1 g/L,FeCl3·6H2O 8 mg/L,Co(NO3)2·6H2O 0.1 mg/L,ZnSO4·7H2O 1mg/L,CuSO4·5H2O 0.1 mg/L, MnSO4·5H2O 0.1 mg/L,接种量为10%,放入恒温摇床中培养,转速150 rpm,温度28 ℃,培养时间为96 h。
表1 不同Co2+的添加量
编号 | 1 | 2 | 3 | 4 | 5 | 6 |
<![CDATA[Co<sup>2+</sup>浓度(mmol/L)]]> | 0 | 1 | 2 | 3 | 4 | 5 |
<![CDATA[CoCl<sub>2</sub>溶液(μL)]]> | 0 | 10 | 20 | 30 | 40 | 50 |
表2 不同Co2+的添加量下中链脂肪酸的产量
<![CDATA[Co<sup>2+</sup>浓度( mmol/L )]]> | 0 | 1 | 2 | 3 | 4 |
中链脂肪酸含量 ( % ) | 1.385 | 4.358 | 9.022 | 7.702 | 7.175 |
实验结果表明,C10和C12总和即中链脂肪酸的含量受到Co2+的影响,Co2+浓度为6mmol/L时卷枝毛霉不生长,在Co2+的添加量为2 mmol/L时有最大值,此时中链脂肪酸所含比例最高,达到占总油脂含量的9.022%。
最佳的Co2+添加时间:
本实验组包含四个完全相同的挡板三角瓶,每个三角瓶中都装有200 mL发酵培养基,最佳Co2+浓度为2 mmol/L,分别在溶液配制时(0h)、一天后(24h)、两天后(48h)、三天后(72h)加入。接种量为10%,放入恒温摇床中培养,转速150 rpm,温度28 ℃,培养时间为96h。
表3 不同Co2+添加时间下中链脂肪酸的产量
<![CDATA[Co<sup>2+</sup>添加时间( d)]]> | 0 | 1 | 2 | 3 |
中链脂肪酸含量 ( % ) | 9.917 | 14.543 | 5.316 | 4.202 |
实验结果表明,当在发酵一天后加入Co2+使得卷枝毛霉中链脂肪酸的含量达到最高,其中的中链脂肪酸占总油脂含量的14.543%。在发酵两天及以后再加入Co2+对其中链脂肪酸产生的促进作用降低,低于在配制培养基时加入Co2+。因此在发酵一天后加入Co2+是最优选择。
发酵罐发酵
种子培养:将储存在-80 ℃ 甘油中的卷枝毛霉WJ11接入种子培养基中,放入恒温摇床中培养,转速150 rpm,温度28 ℃,培养时间为24 h,获得种子液。
本实验采用四个发酵罐同时发酵,编号依次为F1、F2、F3、F4,设置的发酵条件如表2所示,设置发酵罐的转速为700 rpm,pH为6.2,温度为28℃,空气流速为1 vvm,发酵时间为120h。
表4 发酵罐中的发酵条件
编号 | F1 | F2 | F3 | F4 |
种子液(mL) | 100 | 100 | 100 | 100 |
产脂培养基(mL) | 900 | 900 | 900 | 900 |
<![CDATA[Co<sup>2+</sup>浓度(mmol/L)]]> | 0 | 2 | 2 | 1 |
<![CDATA[Co<sup>2+</sup>添加时间(h)]]> | 0 | 0 | 24 | 24 |
表5 发酵罐120 h脂肪酸组成(%)
F1 | F2 | F3 | F4 | |
C10:0 | 0.34±0.05 | 4.27±0.37 | 4.67±0.36 | 4.23±0.37 |
C12:0 | 0.97±0.11 | 9.28±0.91 | 10.62±0.56 | 9.04±0.89 |
C14:0 | 2.05±0.95 | 7.20±0.85 | 7.09±0.74 | 6.15±0.62 |
C16:0 | 33.29±1.2 | 20.02±1.17 | 21.61±1.58 | 21.55±1.57 |
C18:0 | 6.23±0.85 | 34.56±1.45 | 34.97±1.76 | 31.96±1.38 |
C18:1 | 31.56±1.87 | 8.51±0.95 | 7.96±0.82 | 9.81±1.01 |
C18:2 | 12.35±1.21 | 10.28±1.05 | 8.76±0.88 | 10.53±1.07 |
C18:3 | 13.21±1.35 | 5.88±0.36 | 4.33±0.45 | 6.74±0.72 |
表6 发酵罐中链脂肪酸的含量(%)
F1 | F2 | F3 | F4 | |
24h | 0.191 | 1.35 | 0.236 | 0.973 |
48h | 0.714 | 7.573 | 0.809 | 6.949 |
72h | 1.132 | 10.683 | 9.275 | 8.73 |
96h | 1.205 | 12.734 | 13.859 | 11.295 |
120h | 1.31 | 13.553 | 15.29 | 13.267 |
表7 发酵罐中链脂肪酸的产量(mg/L)
F1 | F2 | F3 | F4 | |
24h | 0.700 | 1.545 | 1.054 | 1.228 |
48h | 29.700 | 89.615 | 36.052 | 186.447 |
72h | 68.762 | 375.340 | 505.000 | 421.404 |
96h | 94.201 | 596.570 | 969.578 | 757.936 |
120h | 108.071 | 680.118 | 1109.737 | 902.018 |
从实验结果中可以看出,往培养基中加入Co2+会影响卷枝毛霉中的脂肪酸组成,C10:0、C12:0、C14:0、C18:0的含量相对于对照组有明显的提高,当在1d时加入2 mmol/LCo2+时,卷枝毛霉油脂中的中链脂肪酸含量最高。发酵结束时,1d时加入2 mmol/LCo2+条件下卷枝毛霉产出中链脂肪酸的产量为1109.7 mg/L。
Claims (2)
1.一种提高卷枝毛霉WJ11中链脂肪酸产量的方法,其特征在于向培养基中加入氯化钴溶液,包括以下步骤:
(1)种子培养:将储存在-80 ℃ 甘油中的卷枝毛霉WJ11接入种子培养基中,放入恒温摇床中培养,转速150 rpm,温度28 ℃,培养时间为24 h;
(2)发酵培养:采用发酵罐发酵,将培养好的种子液接入发酵培养基,接种量为10%,添加氯化钴的终浓度为2mmol/L,添加时间为接种后的24h,发酵罐搅拌桨转速为700 rpm, pH为6 .2,空气流速为1vvm,发酵温度为28 ℃,发酵时间为120h。
2.根据权利要求1所述的提高卷枝毛霉WJ11中链脂肪酸产量的方法,其特征在于,
种子培养基的特征为:葡萄糖 30 g/L,MgSO4·7H2O 1.5 g/L,酒石酸铵3.3g/L,KH2PO47 g/L,Na2HPO4 2 g/L,酵母抽提物 1 .5 g/L,CaCl2·2H2O 0 .1 g/L,FeCl3·6H2O 8 mg/L,Co(NO3)2·6H2O 0 .1 mg/L,ZnSO4·7H2O 1 mg/L,CuSO4·5H2O 0 .1 mg/L,MnSO4·5H2O0 .1 mg/L;
发酵培养基的特征为:葡萄糖 80 g/L,MgSO4·7H2O 1 .5 g/L,酒石酸铵2 .0 g/L,KH2PO4 7 g/L,Na2HPO4 2 g/L,酵母抽提物 1 .5 g/L,CaCl2·2H2O 0 .1 g/L,FeCl3·6H2O8 mg/L,Co(NO3)2·6H2O 0 .1 mg/L,ZnSO4·7H2O 1 mg/L,CuSO4·5H2O 0 .1mg/L,MnSO4·5H2O 0 .1 mg/L。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010772667.9A CN111718968B (zh) | 2020-08-04 | 2020-08-04 | 一种提高卷枝毛霉wj11中链脂肪酸产量的方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010772667.9A CN111718968B (zh) | 2020-08-04 | 2020-08-04 | 一种提高卷枝毛霉wj11中链脂肪酸产量的方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN111718968A CN111718968A (zh) | 2020-09-29 |
CN111718968B true CN111718968B (zh) | 2023-04-07 |
Family
ID=72574121
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010772667.9A Expired - Fee Related CN111718968B (zh) | 2020-08-04 | 2020-08-04 | 一种提高卷枝毛霉wj11中链脂肪酸产量的方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111718968B (zh) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114410482A (zh) * | 2022-01-21 | 2022-04-29 | 山东和众康源生物科技有限公司 | 一种用于提高卷枝毛霉WJ11产γ-亚麻酸产量的方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103097540A (zh) * | 2010-05-28 | 2013-05-08 | 索拉兹米公司 | 由重组异养微生物生产的特制油 |
CN104946539A (zh) * | 2014-12-18 | 2015-09-30 | 江南大学 | 一株能够高产脂的卷枝毛霉及应用 |
CN107142288A (zh) * | 2017-07-11 | 2017-09-08 | 江南大学 | 混合菌群发酵合成气产乙酸和辛酸的方法 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8313911B2 (en) * | 2003-05-07 | 2012-11-20 | E I Du Pont De Nemours And Company | Production of polyunsaturated fatty acids in oleaginous yeasts |
-
2020
- 2020-08-04 CN CN202010772667.9A patent/CN111718968B/zh not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103097540A (zh) * | 2010-05-28 | 2013-05-08 | 索拉兹米公司 | 由重组异养微生物生产的特制油 |
CN104946539A (zh) * | 2014-12-18 | 2015-09-30 | 江南大学 | 一株能够高产脂的卷枝毛霉及应用 |
CN107142288A (zh) * | 2017-07-11 | 2017-09-08 | 江南大学 | 混合菌群发酵合成气产乙酸和辛酸的方法 |
Non-Patent Citations (3)
Title |
---|
Engineering of Fatty Acid Synthases (FASs) to Boost the Production of Medium-Chain Fatty Acids (MCFAs) in Mucor circinelloides;Syed Ammar Hussain等;《International Journal of Molecular Sciences》;20190212;第20卷;786 * |
Photosynthesis-dependent biosynthesis of medium chain-length fatty acids and alcohols;Ian Sofian Yunus等;《Metabolic Engineering》;20180725;第49卷;59-68 * |
重金属离子对耶氏解脂酵母油脂积累量及柠檬酸分泌量的影响;张鲁宁等;《食品工业科技》;20191129;第41卷(第10期);89-94,100 * |
Also Published As
Publication number | Publication date |
---|---|
CN111718968A (zh) | 2020-09-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110846346B (zh) | 富含Sn-2位DHA的微生物油脂及其制备方法和应用 | |
CN109971663B (zh) | 一株耐热亚罗解脂酵母及其应用 | |
CN105112463A (zh) | 通过在发酵罐中高密度培养真核微生物来增加含有多烯脂肪酸的脂质的产生 | |
CN102864111B (zh) | 一株产二十二碳六烯酸的裂殖壶菌菌株 | |
CN102899254B (zh) | 裂殖壶菌及其高密度发酵生产dha的方法 | |
CN107164238B (zh) | 一种裂殖壶菌菌株及其诱变方法和应用 | |
CN104278107B (zh) | 一种基于溶氧调控高山被孢霉发酵产花生四烯酸油脂的方法 | |
CN111718968B (zh) | 一种提高卷枝毛霉wj11中链脂肪酸产量的方法 | |
WO2021073011A1 (zh) | 一种生产长链二元酸的菌株及其发酵方法 | |
CN102304479A (zh) | 添加植物激素的培养基及其在裂殖壶菌发酵中的应用 | |
CN106609247B (zh) | 一种羊肚菌的深层发酵培养方法 | |
CN103966273B (zh) | 一种双鞭甲藻发酵生产dha的方法 | |
CN102676594A (zh) | 一种γ-亚麻酸的制备方法 | |
CN104152503B (zh) | 一种提高异养下微藻脂肪酸产率的方法 | |
CN103834698B (zh) | 一种通过温度转换发酵生产含γ‑亚麻酸油脂的方法 | |
CN113005154A (zh) | 一种提高裂殖壶菌中二十碳五烯酸产量的方法 | |
CN108517338B (zh) | 一种基于活性氧调控高山被孢霉发酵产花生四烯酸油脂的方法 | |
CN108587913B (zh) | 一种具有高α-亚麻酸含量的栅藻、其培养方法及其应用 | |
CN111543575A (zh) | 一种可用于食品冷冻的防冻液 | |
CN114940947B (zh) | 一株产dha的裂壶藻gt-d1及其应用、富含dha油脂及其制备方法 | |
CN115161356B (zh) | 一种裂殖壶菌发酵产物及其制备方法与应用 | |
CN107099574B (zh) | 一种用于提高多不饱和脂肪酸产量的复合微生物菌剂 | |
Gu et al. | Effect of temperature and agitation speed on fatty acid accumulation in Mortierella alpina | |
CN117089504B (zh) | 一种发酵植物乳植杆菌的方法 | |
CN110982716B (zh) | 用于生产天然酪醇的菌株及天然酪醇的制备方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20230407 |
|
CF01 | Termination of patent right due to non-payment of annual fee |