CN108424938A - A kind of fermentation medium of thraustochytriale high yield aliphatic acid and its application - Google Patents
A kind of fermentation medium of thraustochytriale high yield aliphatic acid and its application Download PDFInfo
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- 238000000855 fermentation Methods 0.000 title claims abstract description 34
- 230000004151 fermentation Effects 0.000 title claims abstract description 34
- 241001467333 Thraustochytriaceae Species 0.000 title abstract description 4
- 239000002253 acid Substances 0.000 title abstract 3
- 125000001931 aliphatic group Chemical group 0.000 title abstract 3
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 33
- 229930195729 fatty acid Natural products 0.000 claims abstract description 33
- 239000000194 fatty acid Substances 0.000 claims abstract description 33
- 150000004665 fatty acids Chemical class 0.000 claims abstract description 33
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 18
- 235000002639 sodium chloride Nutrition 0.000 claims abstract description 9
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 8
- 239000011780 sodium chloride Substances 0.000 claims abstract description 8
- 229910021642 ultra pure water Inorganic materials 0.000 claims abstract description 8
- 239000012498 ultrapure water Substances 0.000 claims abstract description 8
- 239000001888 Peptone Substances 0.000 claims abstract description 7
- 108010080698 Peptones Proteins 0.000 claims abstract description 7
- 229940041514 candida albicans extract Drugs 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims abstract description 7
- 235000019319 peptone Nutrition 0.000 claims abstract description 7
- 239000012138 yeast extract Substances 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims abstract description 6
- 241000233675 Thraustochytrium Species 0.000 claims description 33
- 238000005303 weighing Methods 0.000 claims description 2
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 claims 1
- 239000002609 medium Substances 0.000 abstract description 31
- 238000004519 manufacturing process Methods 0.000 abstract description 18
- 150000004671 saturated fatty acids Chemical class 0.000 abstract description 13
- 235000011187 glycerol Nutrition 0.000 abstract description 7
- 239000001963 growth medium Substances 0.000 abstract description 6
- 229910000402 monopotassium phosphate Inorganic materials 0.000 abstract description 6
- 235000019796 monopotassium phosphate Nutrition 0.000 abstract description 6
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 3
- SBJKKFFYIZUCET-JLAZNSOCSA-N Dehydro-L-ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(=O)C1=O SBJKKFFYIZUCET-JLAZNSOCSA-N 0.000 abstract 1
- DVSZKTAMJJTWFG-UHFFFAOYSA-N docosa-2,4,6,8,10,12-hexaenoic acid Chemical compound CCCCCCCCCC=CC=CC=CC=CC=CC=CC(O)=O DVSZKTAMJJTWFG-UHFFFAOYSA-N 0.000 description 26
- MBMBGCFOFBJSGT-KUBAVDMBSA-N docosahexaenoic acid Natural products CC\C=C/C\C=C/C\C=C/C\C=C/C\C=C/C\C=C/CCC(O)=O MBMBGCFOFBJSGT-KUBAVDMBSA-N 0.000 description 26
- 239000007788 liquid Substances 0.000 description 6
- 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 description 5
- 210000004027 cell Anatomy 0.000 description 5
- 235000021323 fish oil Nutrition 0.000 description 5
- 239000008103 glucose Substances 0.000 description 5
- 244000005700 microbiome Species 0.000 description 5
- 239000002028 Biomass Substances 0.000 description 4
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 241001643316 Thraustochytriaceae sp. Species 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 241000598397 Schizochytrium sp. Species 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 241001298230 Thraustochytrium sp. Species 0.000 description 2
- 238000009629 microbiological culture Methods 0.000 description 2
- 235000021281 monounsaturated fatty acids Nutrition 0.000 description 2
- ISYWECDDZWTKFF-UHFFFAOYSA-N nonadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCCC(O)=O ISYWECDDZWTKFF-UHFFFAOYSA-N 0.000 description 2
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 description 2
- 235000003441 saturated fatty acids Nutrition 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 208000024172 Cardiovascular disease Diseases 0.000 description 1
- 241000555825 Clupeidae Species 0.000 description 1
- WQZGKKKJIJFFOK-QTVWNMPRSA-N D-mannopyranose Chemical compound OC[C@H]1OC(O)[C@@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-QTVWNMPRSA-N 0.000 description 1
- 229930091371 Fructose Natural products 0.000 description 1
- 239000005715 Fructose Substances 0.000 description 1
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 1
- 208000031226 Hyperlipidaemia Diseases 0.000 description 1
- 206010061218 Inflammation Diseases 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 239000003225 biodiesel Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000004958 brain cell Anatomy 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000011081 inoculation Methods 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 150000003904 phospholipids Chemical class 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 210000001525 retina Anatomy 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000012086 standard solution Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- 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
- C12P7/6427—Polyunsaturated fatty acids [PUFA], i.e. having two or more double bonds in their backbone
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Abstract
Description
技术领域technical field
本发明涉及微生物领域,特别是一种破囊壶菌高产脂肪酸的发酵培养基及其应用。The invention relates to the field of microorganisms, in particular to a thraustochytrium high-yield fatty acid fermentation medium and application thereof.
背景技术Background technique
破囊壶菌(Thraustochytrids)是一类异养的分布广泛的类真菌类海洋原生生物。由于破囊壶菌的细胞内可以累积大量的脂肪酸,可以达到生物质含量的50%以上,包括饱和脂肪酸、单不饱和脂肪酸和多不饱和脂肪酸。其中,饱和脂肪酸和单不饱和脂肪酸是合成生物柴油的主要原料。多不饱和脂肪酸作为细胞膜磷脂的主要成分,是一类对于人体健康不可或缺的营养物质,尤其是DHA(docosahexenoic acid)。DHA可辅助脑细胞和视网膜正常发育,同时DHA还具有预防心血管疾病、高血脂症和抗炎作用。Thraustochytrids are heterotrophic fungi-like marine protists that are widely distributed. Because the cells of Thraustochytrium can accumulate a large amount of fatty acids, which can reach more than 50% of the biomass content, including saturated fatty acids, monounsaturated fatty acids and polyunsaturated fatty acids. Among them, saturated fatty acids and monounsaturated fatty acids are the main raw materials for biodiesel synthesis. As the main component of cell membrane phospholipids, polyunsaturated fatty acids are an indispensable nutrient for human health, especially DHA (docosahexenoic acid). DHA can assist the normal development of brain cells and retina, while DHA also has the effect of preventing cardiovascular disease, hyperlipidemia and anti-inflammation.
在自然界中,DHA主要分布在海洋微生物,特别是生活在深海和寒冷地区的海洋生物。目前,DHA的商业来源主要是海洋鱼油,沙丁鱼、鳍鱼等含有较高的脂肪组织,在很多国家都被用来生产鱼油,鱼油中DHA的含量可以达到20-30%。市售食品级高浓度DHA(27%-30%)价格在73-110万元/吨,2010年中国的DHA总消费量达到2260吨,中国DHA产业拥有非常广阔的发展空间。但是以鱼油为原料生产DHA具有很多缺点,如鱼油具有鱼腥味、成分复杂以及存在潜在的重金属污染等。以微生物作为替代来源,通过微生物发酵培养生产DHA可以有效解决鱼油DHA的生产问题。在有些破囊壶菌菌株的细胞内,其DHA含量可以达到25%以上。通过规模化发酵培养破囊壶菌,获取DHA活性产物,具有污染少成本低等诸多优势。因此,破囊壶菌是DHA工业生产应用的有效来源,其应用前景已受到了国际上的广泛重视。In nature, DHA is mainly distributed in marine microorganisms, especially marine organisms living in deep sea and cold regions. At present, the commercial source of DHA is mainly marine fish oil. Sardines, fin fish, etc. contain high fat tissue, and are used to produce fish oil in many countries. The content of DHA in fish oil can reach 20-30%. The price of commercially available food-grade high-concentration DHA (27%-30%) is 730,000-1.1 million yuan/ton. In 2010, the total consumption of DHA in China reached 2,260 tons. China's DHA industry has a very broad space for development. However, the production of DHA from fish oil has many disadvantages, such as fishy smell, complex composition and potential heavy metal pollution. Using microorganisms as an alternative source to produce DHA through microbial fermentation can effectively solve the production problem of fish oil DHA. In the cells of some Thraustochytrium strains, the DHA content can reach more than 25%. Through large-scale fermentation and cultivation of Thraustochytrium to obtain DHA active products, it has many advantages such as less pollution and low cost. Therefore, Thraustochytrium is an effective source of DHA for industrial production and application, and its application prospect has received extensive attention in the world.
破囊壶菌是是一种异养微生物,培养基的组成对其生长和油脂的累积影响很大,破囊壶菌能够利用葡萄糖、果糖、蔗糖和甘露糖等多种碳源。但是对不同碳源的利用效率差别很大,其中葡萄糖是大多数微生物能够利用的碳源。但是,目前含有葡萄糖的培养基发酵培养破囊壶菌,其脂肪酸的产量也不更理想。Thraustochytrium is a heterotrophic microorganism. The composition of the medium has a great influence on its growth and oil accumulation. Thraustochytrium can utilize various carbon sources such as glucose, fructose, sucrose and mannose. However, the utilization efficiency of different carbon sources varies greatly, among which glucose is the carbon source that most microorganisms can utilize. However, currently, thraustochytrium is fermented and cultured on medium containing glucose, and the yield of fatty acid is not ideal.
发明内容Contents of the invention
本发明的目的是克服现有技术的不足,提供一种低成本,能提高脂肪酸产量的破囊壶菌高产脂肪酸的发酵培养基。The purpose of the invention is to overcome the deficiencies of the prior art, and provide a low-cost, high-fatty-acid-yielding fermentation medium of Thraustochytrium that can increase fatty acid production.
本发明的第二个目的是提供一种破囊壶菌高产脂肪酸的发酵培养基的应用。The second object of the present invention is to provide an application of a thraustochytrium high-yielding fatty acid fermentation medium.
本发明的技术方案概述如下:Technical scheme of the present invention is summarized as follows:
一种破囊壶菌高产脂肪酸的发酵培养基,用下述方法制成:按比例称取甘油45-65g、蛋白胨1-2g、酵母提取物0.5-1.5g、磷酸二氢钾0.2-0.3g、人工海盐25-40g,加超纯水至1000ml,搅拌均匀,115℃灭菌21分钟,冷却至室温,即得。A thraustochytrium high-yield fatty acid fermentation medium, prepared by the following method: weighing 45-65g of glycerin, 1-2g of peptone, 0.5-1.5g of yeast extract, and 0.2-0.3g of potassium dihydrogen phosphate 1. Add 25-40g of artificial sea salt, add ultrapure water to 1000ml, stir evenly, sterilize at 115°C for 21 minutes, cool to room temperature, and get ready.
上述一种破囊壶菌高产脂肪酸的发酵培养基发酵培养破囊壶菌高产脂肪酸的应用。Application of the above-mentioned fermentation medium for thraustochytrium high-yield fatty acid fermentation culture thraustochytrium high-yield fatty acid.
本发明的优点:Advantages of the present invention:
(1)本发明利用甘油,节省生产成本。(1) The present invention utilizes glycerin to save production cost.
(2)使用本发明的培养基与原培养基(通用培养基,含葡萄糖)相比,总脂肪酸、饱和脂肪酸和DHA的产量显著性提高,提高了原料利用效率。(2) Compared with the original culture medium (universal culture medium, containing glucose) using the culture medium of the present invention, the output of total fatty acid, saturated fatty acid and DHA is significantly improved, and the raw material utilization efficiency is improved.
(3)本发明的发酵培养基的发酵条件简单,操作方便,生产成本低,易于大规模发酵生产,节能。(3) The fermentation medium of the present invention has simple fermentation conditions, convenient operation, low production cost, easy large-scale fermentation production, and energy saving.
附图说明Description of drawings
图1为破囊壶菌Schizochytrium sp.PKU#Mn4(CGMCC 8091)利用通用培养基(M4)与本发明实施例1制备的破囊壶菌高产脂肪酸的发酵培养基(简称:MZ)的总脂肪酸、饱和脂肪酸及DHA的产量。Fig. 1 is the total fatty acid of Thraustochytrium sp.PKU#Mn4 (CGMCC 8091) using universal culture medium (M4) and the fermentation medium (abbreviation: MZ) of Thraustochytrium high-yield fatty acid prepared in Example 1 of the present invention , saturated fatty acid and DHA production.
图2为破囊壶菌Thraustochytriidae sp.PKU#Mn16(JX847368.1CGMCC 8095)利用通用培养基(M4)与高产脂肪酸的发酵培养基(MZ)的生物量、总脂肪酸、饱和脂肪酸及DHA的产量。Figure 2 shows the biomass, total fatty acid, saturated fatty acid and DHA production of Thraustochytriidae sp.PKU#Mn16 (JX847368.1CGMCC 8095) using a universal medium (M4) and a high-yield fatty acid fermentation medium (MZ).
具体实施方式Detailed ways
下面通过具体实施例对本发明作进一步的说明。The present invention will be further described below by specific examples.
破囊壶菌Schizochytrium sp.PKU#Mn4(拉丁文:Schizochytrium sp.PKU#Mn4,保藏日期:2014年4月9日,保藏单位:中国微生物菌种保藏管理委员会普通微生物中心(CGMCC),编号:CGMCC 8091)。地址为北京市朝阳区北辰西路1号院3号中国科学院微生物研究所,邮编100101。Thraustochytrium sp.PKU#Mn4 (Latin: Schizochytrium sp.PKU#Mn4, date of deposit: April 9, 2014, depository unit: General Microorganism Center (CGMCC), China Committee for Microbial Culture Collection, number: CGMCC 8091). The address is Institute of Microbiology, Chinese Academy of Sciences, No. 3, Courtyard No. 1, Beichen West Road, Chaoyang District, Beijing, 100101.
破囊壶菌Thraustochytriidae sp.PKU#Mn16(拉丁文:Thraustochytriidaesp.PKU#Mn16,保藏日期:2014年4月9日,保藏单位:中国微生物菌种保藏管理委员会普通微生物中心(CGMCC),编号:CGMCC 8095)。地址为北京市朝阳区北辰西路1号院3号中国科学院微生物研究所,邮编100101。Thraustochytriidae sp.PKU#Mn16 (Latin: Thraustochytriidaesp.PKU#Mn16, date of deposit: April 9, 2014, depository unit: General Microorganism Center (CGMCC), China Committee for Microbial Culture Collection, number: CGMCC 8095). The address is Institute of Microbiology, Chinese Academy of Sciences, No. 3, Courtyard No. 1, Beichen West Road, Chaoyang District, Beijing, 100101.
本发明使用的人工海盐为法国红十字公司生产的小丑盐。但并不对本发明作任何限制。The artificial sea salt used in the present invention is the clown salt produced by French Red Cross Company. But it does not limit the present invention in any way.
实施例1Example 1
一种破囊壶菌高产脂肪酸的发酵培养基(简称MZ),是用下述方法制成:称取甘油60g、蛋白胨1.5g、酵母提取物1g、磷酸二氢钾0.25g、人工海盐33g,加超纯水至1000ml,搅拌均匀,115℃灭菌21分钟,冷却至室温,即得。A thraustochytrium high-yield fatty acid fermentation medium (abbreviated as MZ) is made by the following method: weigh 60g of glycerol, 1.5g of peptone, 1g of yeast extract, 0.25g of potassium dihydrogen phosphate, and 33g of artificial sea salt. Add ultrapure water to 1000ml, stir evenly, sterilize at 115°C for 21 minutes, cool to room temperature, and obtain.
实施例2Example 2
一种破囊壶菌高产脂肪酸的发酵培养基,是用下述方法制成:称取甘油45g、蛋白胨2g、酵母提取物0.5g、磷酸二氢钾0.3g、海盐25g,加超纯水至1000ml,搅拌均匀,115℃灭菌21分钟,冷却至室温,即得。A thraustochytrium high-yield fatty acid fermentation medium is prepared by the following method: Weigh 45g of glycerin, 2g of peptone, 0.5g of yeast extract, 0.3g of potassium dihydrogen phosphate, and 25g of sea salt, and add ultrapure water to 1000ml, stir well, sterilize at 115°C for 21 minutes, cool to room temperature, ready to serve.
实施例3Example 3
一种破囊壶菌高产脂肪酸的发酵培养基,是用下述方法制成:称取甘油65g、蛋白胨1g、酵母提取物1.5g、磷酸二氢钾0.2g、海盐40g,加超纯水至1000ml,搅拌均匀,115℃灭菌21分钟,冷却至室温,即得。A thraustochytrium high-yield fatty acid fermentation medium is made by the following method: Weigh 65g of glycerin, 1g of peptone, 1.5g of yeast extract, 0.2g of potassium dihydrogen phosphate, and 40g of sea salt, add ultrapure water to 1000ml, stir well, sterilize at 115°C for 21 minutes, cool to room temperature, ready to serve.
实施例4Example 4
破囊壶菌通用培养基(简称M4)配方为:葡萄糖20g/l、酵母提取物1g/l、蛋白胨1.5g/l、磷酸二氢钾0.25g/l、海盐33g/l。Thraustochytrium universal medium (referred to as M4) formula is: glucose 20g/l, yeast extract 1g/l, peptone 1.5g/l, potassium dihydrogen phosphate 0.25g/l, sea salt 33g/l.
实施例5Example 5
破囊壶菌高产脂肪酸的发酵培养基发酵培养破囊壶菌高产脂肪酸的应用,包括如下步骤:Thraustochytrium high-yield fatty acid fermentation medium fermentation culture application of Thraustochytrium high-yield fatty acid comprises the following steps:
1.菌株的活化:从固体培养基上挑取破囊壶菌单菌落接种于新的固体培养基上,三区划线,置28℃培养箱中培养48-72h,得活化菌株;1. Activation of the strain: Pick a single colony of Thraustochytrium from the solid medium and inoculate it on a new solid medium, draw a line in three zones, and culture it in an incubator at 28°C for 48-72 hours to obtain an activated strain;
2、破囊壶菌种子液的制备:挑取一环活化破囊壶菌接种于M4培养基中,置150rpm摇床28℃培养24小时,制得破囊壶菌种子发酵液;2. Preparation of Thraustochytrium seed liquid: pick a ring of activated Thraustochytrium and inoculate it in M4 medium, place it on a shaker at 150rpm and incubate at 28°C for 24 hours to prepare Thraustochytrium seed fermentation liquid;
3、接种发酵培养:按接种量为10%接种破囊壶菌种子液于MZ中,在培养温度为28℃的条件下,150rpm摇床培养4天,即可得到破囊壶菌发酵液。3. Inoculation and fermentation culture: inoculate the Thraustochytrium seed liquid in MZ according to the inoculum size of 10%, and cultivate it on a 150rpm shaking table for 4 days at a culture temperature of 28° C. to obtain the Thraustochytrium fermented liquid.
4、生物量的测定:取15ml破囊壶菌发酵液于恒重的50ml离心管中,10000rpm离心10分钟,弃去上清液,下层菌体分别用15ml灭菌超纯水水洗两次,得到破囊壶菌菌体,将菌体放在冻干机中冻干48小时,称重,即可得到发酵液中破囊壶菌的生物量。4. Determination of biomass: Take 15ml of thraustochytrium fermented liquid in a 50ml centrifuge tube with constant weight, centrifuge at 10000rpm for 10 minutes, discard the supernatant, and wash the lower layer of bacteria twice with 15ml of sterilized ultrapure water respectively. Thraustochytrium thallus cells are obtained, and the thallus cells are freeze-dried in a freeze dryer for 48 hours, weighed, and the biomass of the Thraustochytrium in the fermentation liquid can be obtained.
5、脂肪酸含量测定:取冻干的菌体中加入4%硫酸甲醇溶液2ml,加入十九烷酸内标溶液,涡旋震荡20秒混匀,80℃水浴1小时,取出放冷至室温,分别加入1ml超纯水和1ml正己烷,涡旋震荡20秒混匀,4000rpm离心2分钟,取上层正己烷层过0.45μm尼龙膜后气相测定脂肪酸含量,并与脂肪酸混标对比,确定脂肪酸组成。5. Determination of fatty acid content: Add 2ml of 4% methanolic sulfuric acid solution to the freeze-dried cells, add nonadecanoic acid internal standard solution, vortex and oscillate for 20 seconds to mix well, bathe in 80°C water bath for 1 hour, take it out and let it cool to room temperature, Add 1ml of ultrapure water and 1ml of n-hexane respectively, vortex for 20 seconds to mix, centrifuge at 4000rpm for 2 minutes, take the upper layer of n-hexane and pass it through a 0.45μm nylon membrane to measure the fatty acid content by gas phase phase, and compare it with the fatty acid mixed standard to determine the fatty acid composition .
实施例6Example 6
破囊壶菌Schizochytrium sp.PKU#Mn4(CGMCC 8091),进行M4培养基与MZ培养基(实施例1制备)发酵培养。分析样品后可知使用M4培养基发酵培养,96小时后其总脂肪酸产量为:0.82g/l,饱和脂肪酸产量为:0.39g/l,DHA产量为:0.36g/l;而使用MZ培养基进行发酵培养,96小时后其总脂肪酸产量为:1.50g/l,饱和脂肪酸产量为:0.63g/l,DHA产量为:0.74g/l。其总脂肪酸产量显著性提高了82.93%(P=0.004),饱和脂肪酸产量显著性提高了61.54%(P=0.019),DHA产量显著性提高了105.56%(P=0.001)。(见图1)Thraustochytrium Schizochytrium sp.PKU#Mn4 (CGMCC 8091) was fermented on M4 medium and MZ medium (prepared in Example 1). After analyzing the sample, it can be seen that the M4 medium was used for fermentation and cultivation, and after 96 hours, its total fatty acid output was: 0.82g/l, the saturated fatty acid output was: 0.39g/l, and the DHA output was: 0.36g/l; After 96 hours of fermentation, the total fatty acid output was 1.50 g/l, the saturated fatty acid output was 0.63 g/l, and the DHA output was 0.74 g/l. The total fatty acid production significantly increased by 82.93% (P=0.004), the saturated fatty acid production significantly increased by 61.54% (P=0.019), and the DHA production significantly increased by 105.56% (P=0.001). (see picture 1)
实施例7Example 7
破囊壶菌Thraustochytriidae sp.PKU#Mn16(CGMCC 8095),进行M4培养基与MZ培养基(实施例2制备)发酵培养。分析样品后可知使用M4培养基发酵培养,96小时后其总脂肪酸产量为:0.74g/l,饱和脂肪酸产量为:0.41g/l,DHA产量为:0.27g/l;而使用MZ培养基进行发酵培养,96小时后其总脂肪酸产量为:2.05g/l,饱和脂肪酸产量为:0.85g/l,DHA产量为:1.01g/l。其总脂肪酸产量显著性提高了177.03%(P=0.005),饱和脂肪酸产量显著性提高了107.32%(P=0.008),DHA产量显著性提高了274.07%(P=0.003)。(见图2)Thraustochytriidae sp.PKU#Mn16 (CGMCC 8095) was fermented on M4 medium and MZ medium (prepared in Example 2). After analyzing the samples, it can be seen that the M4 medium was used for fermentation and cultivation, and after 96 hours, the total fatty acid output was 0.74g/l, the saturated fatty acid output was 0.41g/l, and the DHA output was 0.27g/l; After 96 hours of fermentation, the total fatty acid output was 2.05g/l, the saturated fatty acid output was 0.85g/l, and the DHA output was 1.01g/l. The total fatty acid production significantly increased by 177.03% (P=0.005), the saturated fatty acid production significantly increased by 107.32% (P=0.008), and the DHA production significantly increased by 274.07% (P=0.003). (See Figure 2)
用实施例3制备的MZ培养基替代本实施例的实施例2制备的MZ培养基,其它同本实施例,MZ培养基进行发酵培养,96小时后其总脂肪酸产量为:2.05g/l,饱和脂肪酸产量为:0.85g/l,DHA产量为:1.01g/l。The MZ medium prepared in Example 3 was used to replace the MZ medium prepared in Example 2 of the present embodiment. Others were the same as in this embodiment. The MZ medium was fermented and cultivated. After 96 hours, its total fatty acid production was: 2.05g/l, Saturated fatty acid yield: 0.85 g/l, DHA yield: 1.01 g/l.
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