CN105132484B - The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA - Google Patents

The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA Download PDF

Info

Publication number
CN105132484B
CN105132484B CN201510609477.4A CN201510609477A CN105132484B CN 105132484 B CN105132484 B CN 105132484B CN 201510609477 A CN201510609477 A CN 201510609477A CN 105132484 B CN105132484 B CN 105132484B
Authority
CN
China
Prior art keywords
algae
dha
algae solution
plant growth
days
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.)
Active
Application number
CN201510609477.4A
Other languages
Chinese (zh)
Other versions
CN105132484A (en
Inventor
孟春晓
李国强
高政权
吴冠勋
郭艳芸
付圣贵
胡硕
沈义成
孙海风
邓素贞
陈国强
张瑞豪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong University of Technology
Original Assignee
Shandong University of Technology
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 Shandong University of Technology filed Critical Shandong University of Technology
Priority to CN201510609477.4A priority Critical patent/CN105132484B/en
Publication of CN105132484A publication Critical patent/CN105132484A/en
Application granted granted Critical
Publication of CN105132484B publication Critical patent/CN105132484B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The present invention provides the method for induction chlorella vulgaris ZF algae strain efficient accumulation DHA a kind of, it is characterized in that using following steps: 1) preparing algae solution: under conditions of 23 DEG C ± 2 DEG C, 1900 ± 100lx of light intensity and Light To Dark Ratio is 12h/12h, logarithmic growth phase is arrived within BG11 culture medium culture chlorella vulgaris ZF algae strain cell 28 days using 1/4 times, the algae solution for plant growth regulator induction is obtained, the BG11 nutritive salt of 1 times of concentration is added within every 14 days during culture;2) accumulate DHA: logarithmic growth phase algae solution 200mL is placed in 300mL triangular pyramidal bottle, then plant growth regulator 6-BA is added, concentration of the plant growth regulator 6-BA in algae solution is 0.01 ± 0.001mg/L, induction processing 14 ± 1 days is carried out in 23 DEG C ± 2 DEG C, processing stage manually shakes algae daily and is no less than 3 times, adjacent algae time interval of shaking realized accumulation of the DHA in algae solution not less than 2 hours.The invention is simple and feasible, low in cost, can significantly accumulate DHA content in a short time.

Description

The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA
Technical field
The present invention provides the method for induction chlorella vulgaris ZF algae strain efficient accumulation DHA a kind of, belongs to field of biotechnology.
Background technique
Chlorella (Chlorella) is a kind of common aquatic unicellular alga, is a weight in green alga chlorella section Belong to, ecologicaI distribution is extensive, is distributed in seawater and fresh water, at present includes about 10 kinds.Contain in chlorella cells Protein (the 50% of dry weight) abundant, essential amino acid, polysaccharide, lipid (result of fatty acid accumulation), chlorophyll, carrot Element and vitamin etc., are widely used in health food, aquaculture (feed addictive), cosmetics, medicine and other fields, Supply falls short of demand for domestic and international market.Compared with the countries such as the U.S., Japan, Israel, the chlorella in China industrializes large-scale culture Level relatively lags behind.Chlorella vulgaris ZF algae strain is a kind of spherical unicellular fresh water algae, is usually grown in the water of eutrophication In body, but can raised growth breeding under culture conditions.Nutritive salt (nitrogen, phosphorus etc.), illumination, pH value, temperature, microelement (iron, manganese, selenium etc.), ammonium hydrogen carbonate, etc. factors can influence chlorella growth.
All-cis formula-7,10,13,16,19-docosahexaenoic acids (docosahexaenoic cid, abbreviation DHA), custom It is the polyunsaturated fatty acid that a kind of pair of human body has extremely important effect at docosapentaenoic acid is in omega-3 unsaturated fatty acid family Important member, dynamic and people itself, which cannot synthesize, to be taken in from the external world.DHA has important physiological action: with antitumor immune It is related, while having the effects that cerebrum tonifying brain tonic, improve eyesight, is reducing blood lipid, blood pressure lowering, antiatherosclerosis, anti-inflammatory, have very big Application value.DHA is mainly obtained from fish oil at present, but the product fishy smell in fish oil source is larger, and quality is not high, and yield is unstable It is fixed.Recently the hot spot studied both at home and abroad is had become by microalgae extraction purification DHA, EPA.Plant growth regulator is plant The chemical substance that regulating and controlling effect is played to plant growth and development of interior generation, can be divided into five major class: auxins, the basic element of cell division Class, gibberellin class, abscisic acid and ethylene, and this five major class growth regulator is equal it has been found that plant growth regulating in algae Agent has apparent facilitation to the growth and development of plant and is widely used in agricultural production.Plant growth regulator conduct One plant growth regulators, with easy to operate, inductivity is high, speed is fast, low cost, damages light, pollution-free, high safety Many advantages, such as.Microalgae is the excellent material for carrying out growth regulator induction, structure is simple, life cycle is short, light sensitivity is strong, Metabolic process is easily affected by environment, is also easy to be detected.
Currently, the relevant technologies of some purifications, the method and process for preparing DHA have been disclosed in foreign countries, most of is needle To technique improvements such as some purifications, separation.As Shandong Inst. of Marine Medicinal Sci. discloses one kind from marine growth grease Middle separation prepares the method (CN88101811) of eicosapentaenoic acid, docosahexaenoic acid or its esters, is sending bright work elsewhere In skill, alkali metal crystallisation and urea inclusion method are improved, and is combined, removed with preceding method full in degreasing The non-isomerization of high-content is thus made with the low unsaturated fatty acid of rear method removing with oil-soluble impurities such as fatty acid and cholesterol EPA, DHA or its ester derivative.A kind of method that EPA and DHA is extracted from seaweed of Lv Weixue invention (CN201110106175), manufacture craft, which is followed successively by, crushes seaweed raw material, and hydrochloric acid hydrolysis is added, grinds and is homogenized through colloid mill Afterwards, successively into ultrafiltration, nanofiltration I, nanofiltration II is crossed, ethyl alcohol is extracted.As Harbin Patent Technique Development Corp. provides one kind with fish Oil is the method (CN88106038) of waste eicosapentaenoic acid, docosahexaenoic acid and its esters, this method product Middle EPA, DHA content are high, and product yield is high.Inner Mongolia Kingdomway Pharmaceutical Co., Ltd. and the limited public affairs of Xiamen Jin Dawei group share Department provides a kind of method (CN200910159368) that DHA unsaturated fatty acid is extracted from dino flagellate fermentation liquor, special Sign is: the hydrochloric acid solution of dino flagellate fermentation liquor mass concentration 10-30% first being adjusted pH value to 3-6, with fermentating liquid volume The noresidue monomer cationic polyacrylamide aqueous solution that 2-5%, concentration are 0.1-0.5% is flocculant flocculation, plate-frame filtering Obtain filter cake, the shell-broken liquid broken wall of 5-10 times of weight of filter cake realizes slag, water phase, oily phase three-phase with supercentrifuge after broken wall Separation, substantially oil-free phase after repeating 2-5 times merge oil mutually and are after washing crude oil containing DHA, and DHA crude oil enters five cascades Continuous molecular distillation, the heavy constituent of prime are directly entered rear class and are distilled, absolute pressure 0.5-5Pa, and 120-140 DEG C of temperature, most The unsaturated fatty acid of DHA must be contained eventually.Hubei Fuxing Biological Technology Co., Ltd. discloses a kind of hidden dinoflagellate of Kou Shi The method of (Crypthecodinium cohnii) industrial fermentation production docosahexaenoic acid grease (CN200910061833).This method provides a kind of is with the hidden dinoflagellate of Kou Shi (Crypthecodinium cohnii) original strain Strain, the method that industrial fermentation produces docosahexaenoic acid grease, this method can be inexpensive, mass production high-content Triglyceride type DHA grease.Above-mentioned related purification, the related patents technology for the method and process for preparing DHA are although advanced, but not It is related to the content of plant growth regulator induction chlorella vulgaris accumulation DHA, and technical matters is relative complex, and costly, this Undoubtedly increase the difficulty of production cost and Technique Popularizing.
Summary of the invention
The object of the present invention is to provide it is a kind of it is easy to operate, speed is fast, low cost, pollution-free, high safety induction are general The method of logical chlorella ZF algae strain efficient accumulation DHA.Its specific technical solution are as follows:
A method of passing through induction chlorella vulgaris ZF algae strain efficient accumulation DHA, it is characterised in that use following steps:
1) it prepares algae solution: under conditions of 23 DEG C ± 2 DEG C, 1900 ± 100lx of light intensity and Light To Dark Ratio are 12h/12h, using 1/4 times is arrived logarithmic growth phase in BG11 culture medium culture chlorella vulgaris ZF algae strain cell 28 days, is obtained and is used for plant growth regulating The algae solution of agent induction, adds the BG11 nutritive salt of 1 times of concentration for every 14 days during culture;
2) accumulate DHA: logarithmic growth phase algae solution 200mL is placed in 300mL triangular pyramidal bottle, and plant growth is then added Concentration of regulator 6-BA, the 6-BA element in algae solution is 0.01 ± 0.001mg/L, and induction processing 14 ± 1 is carried out in 23 DEG C ± 2 DEG C It, processing stage manually shakes algae daily and is no less than 3 times, and adjacent algae time interval of shaking realized DHA in algae solution not less than 2 hours Accumulation.
Compared with prior art, the present invention its advantage is that:
1, simple and easy, raw material chlorella vulgaris ZF algae strain cell is easy to cultivate, and the period is short, at low cost.
2, the intracellular DHA content of chlorella vulgaris ZF algae strain can be significantly improved, the results showed that, after induction processing, DHA content It is 1.22-the 1.29% of frustule dry weight, is 7.21-7.62 times of cellular control unit respectively.
Specific embodiment
Embodiment 1, using following steps:
1) it prepares algae solution: under conditions of 23 DEG C, light intensity 1800lx and Light To Dark Ratio are 12h/12h, being trained using 1/4 times of BG11 It supports the strain of base culture chlorella vulgaris ZF algae and arrives logarithmic growth phase in cell 28 days, obtain the algae for plant growth regulator induction Liquid adds the BG11 nutritive salt of 1 times of concentration for every 14 days during culture;
2) accumulate DHA: logarithmic growth phase algae solution 200mL is placed in 300mL triangular pyramidal bottle, and Beijing Suo Lai is then added The plant growth regulator 6-BA of precious Science and Technology Ltd.'s production, makes concentration of the plant growth regulator 6-BA in algae solution 0.01mg/L carries out induction processing 14 days in 23 DEG C, and processing stage manually shakes algae daily and is no less than 3 times, adjacent to shake between the algae time Every being not less than 2 hours, accumulation of the DHA in algae solution is realized.
Embodiment 2, using following steps:
1) it prepares algae solution: under conditions of 24 DEG C, light intensity 2000lx and Light To Dark Ratio are 12h/12h, being trained using 1/4 times of BG11 It supports the strain of base culture chlorella vulgaris ZF algae and arrives logarithmic growth phase in cell 28 days, obtain the algae for plant growth regulator induction Liquid adds the BG11 nutritive salt of 1 times of concentration for every 14 days during culture;
2) accumulate DHA: logarithmic growth phase algae solution 200mL is placed in 300mL triangular pyramidal bottle, and Beijing Suo Lai is then added The plant growth regulator 6-BA of precious Science and Technology Ltd.'s production, makes concentration of the plant growth regulator 6-BA in algae solution 0.011mg/L carries out induction processing 15 days in 24 DEG C, and processing stage manually shakes algae daily and is no less than 3 times, adjacent to shake between the algae time Every being not less than 2 hours, accumulation of the DHA in algae solution is realized.
Experiment detection:
1) be enriched with frustule: 8000-9000rpm, 4 DEG C centrifugation 5-8 minutes, obtain bath mud, then by algal gel in -40 DEG C of freezings Dry algae powder.
2) it extracts grease: the algae powder after freeze-drying being extracted to get grease using soxhlet extraction.
3) to grease esterification: 3ml 0.4mol/L KOH/ methanol, 60 DEG C of water being added first into the total grease extracted Bathe 1h;14%BF is added after cooling3·CH3OH solution 3ml, 60 DEG C of water-bath 1h;20 μ L 10mg/mL nonadecanoic acids are added after cooling down again Methyl esters, 1ml n-hexane (chromatographically pure) and 1ml are saturated NaCl, and stratification after anhydrous sodium sulfate is added, on 1ml syringe extracts Layer organic phase, is stored in 1.5mL EP after filtering.
4) DHA content is analyzed: it is analyzed using chromatography of gases, chromatographic column is the anti-oxidant crosslinking quartz capillary column of HP-FFAP, Specification is 30m × 0.25mm × 0.3m;Injector temperature is 260 DEG C, split ratio 50: 1;Carrier gas is high-purity N 2, and column flow is 1mL/min, total flow 55mL/min, pressure 114Kpa, linear velocity 29.6cm/s, column temperature is by 160 DEG C of speed liters with 2 DEG C/min To 230 DEG C, holding 3min to appearance is finished;Fid detector, temperature are 230 DEG C, and sample volume 1uL obtains chromatography of gases figure.Meter Calculate result are as follows: 1 gained DHA content of embodiment is frustule dry weight 1.22%, is 7.21 times of cellular control unit, 2 institute of embodiment 1.29% that DHA content is frustule dry weight is obtained, is 7.62 times of cellular control unit.

Claims (1)

1. a kind of method of induction chlorella vulgaris ZF algae strain efficient accumulation DHA, it is characterised in that use following steps:
1) algae solution is prepared: under conditions of 23 DEG C ± 2 DEG C, 1900 ± 100lx of light intensity and Light To Dark Ratio are 12h/12h, using 1/4 times It arrives logarithmic growth phase within BG11 culture medium culture chlorella vulgaris ZF algae strain cell 28 days, obtains and induced for plant growth regulator Algae solution, the BG11 nutritive salt of every 14 days plus 1 times of concentration during culture;
2) accumulate DHA: logarithmic growth phase algae solution 200mL is placed in 300mL triangular pyramidal bottle, and plant growth regulating is then added The concentration of agent 6-BA, plant growth regulator 6-BA in algae solution is 0.01 ± 0.001mg/L, is induced in 23 DEG C ± 2 DEG C Processing 14 ± 1 days, processing stage manually shakes algae daily and is no less than 3 times, and adjacent algae time interval of shaking realized DHA not less than 2 hours Accumulation in algae solution.
CN201510609477.4A 2015-09-23 2015-09-23 The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA Active CN105132484B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510609477.4A CN105132484B (en) 2015-09-23 2015-09-23 The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510609477.4A CN105132484B (en) 2015-09-23 2015-09-23 The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA

Publications (2)

Publication Number Publication Date
CN105132484A CN105132484A (en) 2015-12-09
CN105132484B true CN105132484B (en) 2019-04-19

Family

ID=54718052

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510609477.4A Active CN105132484B (en) 2015-09-23 2015-09-23 The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA

Country Status (1)

Country Link
CN (1) CN105132484B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103305560A (en) * 2013-06-06 2013-09-18 山东理工大学 Method for inducing fresh water chlorella to fast accumulate grease through plant hormone jasmonic acid
WO2014081963A2 (en) * 2012-11-21 2014-05-30 Nair, Ramesh Engineering plants to produce farnesene and other terpenoids

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014081963A2 (en) * 2012-11-21 2014-05-30 Nair, Ramesh Engineering plants to produce farnesene and other terpenoids
CN103305560A (en) * 2013-06-06 2013-09-18 山东理工大学 Method for inducing fresh water chlorella to fast accumulate grease through plant hormone jasmonic acid

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Enhancement of microalgae growth and fatty acid content under the influence of phytohormones;El-Sayed Salama,et al.;《Bioresource Technology》;20141130;第172卷;第97–103页
蹄形藻和单针藻生长与油脂合成影响因素的研究;徐阳;《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》;20140215(第2期);第6页第3-8段,第46-49页3.3.10部分以及表3.20,表3.21

Also Published As

Publication number Publication date
CN105132484A (en) 2015-12-09

Similar Documents

Publication Publication Date Title
Enamala et al. Production of biofuels from microalgae-A review on cultivation, harvesting, lipid extraction, and numerous applications of microalgae
Dolganyuk et al. Microalgae: A promising source of valuable bioproducts
Liu et al. Carotenoids from fungi and microalgae: A review on their recent production, extraction, and developments
Santos-Sánchez et al. Lipids rich in ω-3 polyunsaturated fatty acids from microalgae
KR102148333B1 (en) Method for continuously enriching an oil produced by microalgae with ethyl esters of dha
CN105821088A (en) Method for preparing glyceride rich in EPA and DHA through enzyme catalysis
US20180042839A1 (en) Omega-7 fatty acid composition, methods of cultivation of tribonema for production of composition and application of composition
CN1986822A (en) Crypthecodinium connii fermenting process for producing docosahexaenoic acid grease
Ummalyma et al. Biomass production and phycoremediation of microalgae cultivated in polluted river water
CN103965143A (en) Method for extracting and separating fucoxanthin from marine unicellular diatom
JP2016509483A (en) Biomass of microalgae Schizochytrium mangrobei and method for preparing the same
Chen et al. Microalgal polyunsaturated fatty acids: Hotspots and production techniques
Chen et al. Screening of red algae filaments as a potential alternative source of eicosapentaenoic acid
Shao et al. Cocamidopropyl betaine-assisted foam separation of freshwater microalgae Desmodesmus brasiliensis
CN102887821B (en) A kind of method of extracting and separating marine microalgae broth extraction DHA
CN105132480B (en) The method for inducing chlorella vulgaris ZF algae strain efficient accumulation EPA
CN105132484B (en) The method for inducing chlorella vulgaris ZF algae strain efficient accumulation DHA
CN110004188A (en) A method of preparing PUFAs glyceride from the crude oil that microbial fermentation obtains
WO2012065545A1 (en) Microalgae culturing method for oil and lutein rapid accumulation
AU2013258928A1 (en) Method for producing lipid
CN103086873A (en) Preparation method of high-purity DHA (Docosahexaenoic Acid) by means of high-speed counter-current chromatography separation
CN105331670B (en) Split the method for pot algae Yu the hidden dinoflagellate mixed fermentation of Kou Shi
JP2002238545A (en) Method for producing chlorella and highly unsaturated fatty acid-containing compound lipid, phospholipid or glycolipid obtained by the production method, food, food additive
CN105132483B (en) Induce the chlorella vulgaris ZF algae strain arachidonic method of efficient accumulation
CN103588634A (en) Method for extracting DHA from marine microalgae fermentation liquor through extraction separation

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant