CN106834137A - A kind of arachidonic microbial fermentation processes - Google Patents

A kind of arachidonic microbial fermentation processes Download PDF

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CN106834137A
CN106834137A CN201611268294.1A CN201611268294A CN106834137A CN 106834137 A CN106834137 A CN 106834137A CN 201611268294 A CN201611268294 A CN 201611268294A CN 106834137 A CN106834137 A CN 106834137A
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崔悦
刘广宁
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Xinchang County Tishman Technology Co Ltd
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    • C12N1/00Microorganisms, 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
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    • C12P7/64Fats; 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
    • C12P7/6409Fatty acids
    • C12P7/6427Polyunsaturated fatty acids [PUFA], i.e. having two or more double bonds in their backbone

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Abstract

A kind of arachidonic microbial fermentation processes, it is characterised in that solid medium is made up of following raw material:Beef extract-peptone, dusty yeast, maltose, vitamin A, vitamin K, sodium chloride, octyl methoxycinnamate, wheat flour;Fermentation medium is made up of following raw material:Maltose, beef extract-peptone, dusty yeast, sodium nitrate, potassium chloride, 12 hydrated sulfuric acid hydrogen potassium, vitamin B12, vitamin K, sodium acid carbonate, water.The arachidonic acid parent species obtained by solid material culture, the growth vigor of bacterium cell is strong, synchronism is preferable, physiological status is stable;By the optimization to zymotechnique, shorten fermentation series, simplify zymotechnique, effectively reduce fermenting and producing cost, arachidonic acid stable yield has recovery rate higher.

Description

A kind of arachidonic microbial fermentation processes
Technical field
The present invention relates to a kind of arachidonic microbial fermentation processes, belong to field of microbial fermentation.
Background technology
Arachidonic acid, is all-cis formula-Arachidonic Acid, belongs to unrighted acid, wherein containing Four carbon-to-carbon double bonds, a carbon-oxygen double bond, is higher unsaturated fatty acid.It is distributed widely in the animal kingdom, certain is present on a small quantity In the glyceride of individual kind, can also be found in glycerophosphatide class.Can be synthesized by linoleic acid in human body.Infer that it is prostaglandin life One of starting material of thing synthesis.
Arachidonic acid (Arachidonicacid) is Arachidonic acid, it be a kind of multivalence not Saturated fatty acid, also referred to as Arachidonic acid, abbreviation ARA or AA.
Arachidonic acid is a kind of important essential fatty acid, itself can not be synthesized in vivo, it is necessary to supplied by food Give, be the important precursor of human prostate's element synthesis, be also content highest in human body, be distributed a kind of most wide how unsaturated Aliphatic acid, is primarily present in organ muscle and blood tissues, and being combined into struetural lipid with phosphatide plays an important role.Peanut four Olefin(e) acid regulation cardiac excitability, participate in neuroendocrine, promote cell division, suppress platelet aggregation, anti-inflammatory, anticancer, Lipid peroxidation inhibition, promote brain development and protection eyesight etc. the aspect there is the bioactivity of uniqueness, be widely used in food, The field such as cosmetics, feed and its additive, babies ' formula milk powder, bio-pharmaceuticals.Arachidonic acid is widely present in animal body In, adrenal gland, liver and sardine, egg yolk of animal etc. are mainly derived from, but content is relatively low, generally below 0.2% (wt/ wt)。
Because the arachidonic acid in human body is absorbed mainly by from the external world, so strengthening to arachidonic research and development Have a very important role.Current people mainly obtain arachidonic acid using microbe fermentation method, and the expansion of seed is trained Foster is the committed step of fermenting and producing, and the quality of parent species quality plays vital effect to the quality of production and yield, but existing The most of parent species for having production arachidonic acid oil in technology are all to use liquid fermentation and culture method, in the product of acquisition still Exist in grease that arachidonic acid content is relatively low, the growth of microorganism cycle is long, culture process is not up to optimization or fermentation institute The problems such as culture medium cost of use is high, limits arachidonic large-scale industrial production.
The content of the invention
It is an object of the invention to provide a kind of arachidonic microbial fermentation processes, the liquid of its abandoning tradition is sent out Ferment cultural method, using solid material culture arachidonic acid parent species, the growth vigor that obtains bacterium cell is strong, synchronism preferably, it is raw Reason is in stable condition, can be mushroomed out after culture transferring to fermentation tank, shortens period of delay, and can keep the product recovery rate of stabilization.
The present invention is achieved in that described a kind of arachidonic microbial fermentation processes, its solid medium It is made up of following raw material:Beef extract-peptone, dusty yeast, maltose, vitamin A, vitamin K, sodium chloride, methoxy cinnamic acid Monooctyl ester, wheat flour.
Specifically, being made up of following raw material and its parts by weight, contain in every 100g culture mediums:Beef extract-peptone 30- 50g, dusty yeast 5-10g, maltose 20-25g, vitamin A 0.5-1g, vitamin K 0.25-0.5g, sodium chloride 1.2g, methoxyl group Cinnamic acid monooctyl ester 0.5-0.8g, wheat flour are supplied.Octyl methoxycinnamate can improve the production effect of culture medium in the medium Rate, strengthens bacterial activity, prevents culture medium aging.
Fermentation medium is made up of following raw material:Maltose, beef extract-peptone, dusty yeast, sodium nitrate, potassium chloride, ten Two hydrated sulfuric acid hydrogen potassium, vitamin B12, vitamin K, sodium acid carbonate, water.
Specifically, above-mentioned fermentation medium is made up of following raw material and its parts by weight, contain in every 100g culture mediums:Wheat Bud sugar 10-15g, beef extract-peptone 30-50g, dusty yeast 10-15g, sodium nitrate 1-3g, potassium chloride 1-2g, 12 hydrated sulfuric acids Hydrogen potassium 0.5-1g, vitamin B120.25-0.5g, vitamin K 0.1-0.2g, sodium acid carbonate 1-2g, water are supplied.
It is as described below present invention also offers a kind of specific steps of arachidonic microbial fermentation processes:
(1)Seed culture is expected in the common Mortierella fermentation of producing arachidonic acid admittedly
(ⅰ)Actication of culture:Activated using slant strains, test tube slant culture medium is PDA solid mediums, by producing arachidonic acid Common Mortierella strain be connected to PDA inclined-planes, 24-26 DEG C is cultivated 2-3 days.
(ⅱ)Admittedly expect the preparation of seed culture medium:Above-mentioned solid medium dispensing is mixed in proportion, 80-100 DEG C of boiling 20-30min, dries to not conglomeration of scattering, and is dispensed into specification as in KShi bottles of 1000mL, 121 DEG C sterilize by 200g/ bottles 30min。
(ⅲ)Admittedly expect the culture of seed:Fresh slant strains are added into spore under the aseptic washings of 15-25mL, spore is made and is hanged Liquid, pours into the solid material culture medium that sterilized, and jog makes its mixing of trying one's best, and is cultivated 2-3 days in 24-26 DEG C, respectively at 12h and 24h Respectively shake up once, as the parent species of one grade fermemtation.
(2)Fermented and cultured
(ⅰ)The preparation of fermentation medium, it is 5.8-6.0,121 DEG C of sterilizings that above-mentioned fermentation medium each component is mixed into regulation pH 30min。
(ⅱ)Shake flask fermentation culture, i.e. sample fermented and cultured
With the above-mentioned spore for expecting the surface of the seed admittedly under the aseptic washings of 200-300ml, spore suspension is made, is 5- by percent by volume 10% inoculum concentration accesses Medium of shaking flask fermentation, and cultivation temperature is 26-30 DEG C, and shaking speed 150-200r/min is cultivated 3-5 days; Wet thallus are collected after fermentation ends, the grease extracted after drying in dry mycelium carries out gas chromatographic detection, detects arachidonic acid Recovery rate.
(ⅲ)Ferment tank culture, i.e., middle sample fermented and cultured:With above-mentioned solid material kind sublist under the aseptic washings of 200-300ml The spore in face, is made spore suspension, is that 5-10% inoculum concentrations access one grade fermemtation tank by percent by volume, and fermentation temperature is 26-30 DEG C, cultivate 1.5-2.5 days;One grade fermemtation to the inoculum concentration percent by volume of second order fermentation is 10-20%, fermentation temperature early stage control System promotes thalli growth at 26-30 DEG C, and temperature, to promote arachidonic acid oil synthesis, is adjusted downward to 18-20 DEG C, training by the later stage The cycle of supporting is 3-4.5 days;The need for ensure thalli growth and Synthetic Oil, whole fermentation process is except auto-feeding is through 118 DEG C The percentage by weight of sterilizing 25min is 40% glucose solution, and percentage by weight is that 28% ammoniacal liquor is used to control reduced sugar to exist Preceding 40h is added auxiliary to be that 3-8g/L and pH is outside 5.8-6.0, to be additionally carried out 2 times and add auxiliary material manually after 6-8g/L, 40h The material time is respectively fermentation 36h and 69h, and auxiliary material is respectively by glucose, soybean-cake flour, corn starch, olive oil, dipotassium hydrogen phosphate And all kinds of trace element compositions, trace element can be vitamin B1, vitamin B2, vitamin B6, vitamin B12, nicotinic acid, cigarette The combination of one or more in acid amide, calcium pantothenate, folic acid, biotin, chlorophyll;Wet thallus are collected after fermentation ends, is dried The grease extracted afterwards in dry mycelium carries out gas chromatographic detection, detects arachidonic acid recovery rate.
The beneficial effects of the invention are as follows the arachidonic acid parent species obtained by solid material culture, the growth of bacterium cell is lived Power is strong, synchronism is preferable, physiological status is stable;By the optimization to zymotechnique, shorten fermentation series, simplify zymotechnique, Fermenting and producing cost is effectively reduced, arachidonic acid stable yield has recovery rate higher.
Specific embodiment
A kind of arachidonic microbial fermentation processes of the present invention, are iurther discussed by following examples.
Embodiment 1
A kind of arachidonic microbial fermentation processes, its solid medium is made up of following raw material and its parts by weight, often Contain in 100g culture mediums:Beef extract-peptone 45g, dusty yeast 6g, maltose 24g, vitamin A 0.6g, vitamin K 0.27g, Sodium chloride 1.2g, octyl methoxycinnamate 0.7g, wheat flour are supplied.
A kind of arachidonic microbial fermentation processes, its fermentation medium is by following raw material and its weight portion array Into, per 100g culture mediums in contain:Maltose 11g, beef extract-peptone 36g, dusty yeast 14g, sodium nitrate 2g, potassium chloride 2g, 12 hydrated sulfuric acid hydrogen potassium 0.8g, vitamin B120.29g, vitamin K 0.15g, sodium acid carbonate 2g, water are supplied.
Embodiment 2
A kind of arachidonic microbial fermentation processes, its solid medium is made up of following raw material and its parts by weight, often Contain in 100g culture mediums:Beef extract-peptone 42g, dusty yeast 8g, maltose 25g, vitamin A 0.5g, vitamin K 0.5g, Sodium chloride 1.2g, octyl methoxycinnamate 0.8g, wheat flour are supplied.
A kind of arachidonic microbial fermentation processes, its fermentation medium is by following raw material and its weight portion array Into, per 100g culture mediums in contain:Maltose 10g, beef extract-peptone 50g, dusty yeast 15g, sodium nitrate 3g, potassium chloride 2g, 12 hydrated sulfuric acid hydrogen potassium 1g, vitamin B120.5g, vitamin K 0.2g, sodium acid carbonate 2g, water are supplied.
Embodiment 3
A kind of arachidonic microbial fermentation processes, its solid medium is made up of following raw material and its parts by weight, often Contain in 100g culture mediums:Beef extract-peptone 30g, dusty yeast 5g, maltose 25g, retinol1 g, vitamin K 0.5g, chlorine Change sodium 1.2g, octyl methoxycinnamate 0.5g, wheat flour to supply.
A kind of arachidonic microbial fermentation processes, its fermentation medium is by following raw material and its weight portion array Into, per 100g culture mediums in contain:Maltose 15g, beef extract-peptone 37g, dusty yeast 15g, sodium nitrate 2.5g, potassium chloride 1.5g, 12 hydrated sulfuric acid hydrogen potassium 0.8g, vitamin B120.26g, vitamin K 0.17g, sodium acid carbonate 1.5g, water are supplied.
A kind of specific steps of arachidonic microbial fermentation processes, it is as described below:
(1)Seed culture is expected in the common Mortierella fermentation of producing arachidonic acid admittedly
(ⅰ)Actication of culture:Activated using slant strains, test tube slant culture medium is PDA solid mediums, by producing arachidonic acid Common Mortierella strain be connected to PDA inclined-planes, 24-26 DEG C is cultivated 2-3 days.
(ⅱ)Admittedly expect the preparation of seed culture medium:Above-mentioned solid medium dispensing is mixed in proportion, 80-100 DEG C of boiling 20-30min, dries to not conglomeration of scattering, and is dispensed into specification as in KShi bottles of 1000mL, 121 DEG C sterilize by 200g/ bottles 30min。
(ⅲ)Admittedly expect the culture of seed:Fresh slant strains are added into spore under the aseptic washings of 15-25mL, spore is made and is hanged Liquid, pours into the solid material culture medium that sterilized, and jog makes its mixing of trying one's best, and is cultivated 2-3 days in 24-26 DEG C, respectively at 12h and 24h Respectively shake up once, as the parent species of one grade fermemtation.
(2)Fermented and cultured
(ⅰ)The preparation of fermentation medium, it is 5.8-6.0,121 DEG C of sterilizings that above-mentioned fermentation medium each component is mixed into regulation pH 30min。
(ⅱ)Shake flask fermentation culture, i.e. sample fermented and cultured
With the above-mentioned spore for expecting the surface of the seed admittedly under the aseptic washings of 200-300ml, spore suspension is made, is 5- by percent by volume 10% inoculum concentration accesses Medium of shaking flask fermentation, and cultivation temperature is 26-30 DEG C, and shaking speed 150-200r/min is cultivated 3-5 days; Wet thallus are collected after fermentation ends, the grease extracted after drying in dry mycelium carries out gas chromatographic detection, detects arachidonic acid Recovery rate.
(ⅲ)Ferment tank culture, i.e., middle sample fermented and cultured:With above-mentioned solid material kind sublist under the aseptic washings of 200-300ml The spore in face, is made spore suspension, is that 5-10% inoculum concentrations access one grade fermemtation tank by percent by volume, and fermentation temperature is 26-30 DEG C, cultivate 1.5-2.5 days;One grade fermemtation to the inoculum concentration percent by volume of second order fermentation is 10-20%, fermentation temperature early stage control System promotes thalli growth at 26-30 DEG C, and temperature, to promote arachidonic acid oil synthesis, is adjusted downward to 18-20 DEG C, training by the later stage The cycle of supporting is 3-4.5 days;The need for ensure thalli growth and Synthetic Oil, whole fermentation process is except auto-feeding is through 118 DEG C The percentage by weight of sterilizing 25min is 40% glucose solution, and percentage by weight is that 28% ammoniacal liquor is used to control reduced sugar to exist Preceding 40h is added auxiliary to be that 3-8g/L and pH is outside 5.8-6.0, to be additionally carried out 2 times and add auxiliary material manually after 6-8g/L, 40h The material time is respectively fermentation 36h and 69h, and auxiliary material is respectively by glucose, soybean-cake flour, corn starch, olive oil, dipotassium hydrogen phosphate And all kinds of trace element compositions, trace element can be vitamin B1, vitamin B2, vitamin B6, vitamin B12, nicotinic acid, cigarette The combination of one or more in acid amide, calcium pantothenate, folic acid, biotin, chlorophyll;Wet thallus are collected after fermentation ends, is dried The grease extracted afterwards in dry mycelium carries out gas chromatographic detection, detects arachidonic acid recovery rate.
Embodiment 4
A kind of arachidonic microbial fermentation processes, its solid medium is made up of following raw material and its parts by weight, often Contain in 100g culture mediums:Beef extract-peptone 40g, dusty yeast 6g, maltose 22g, vitamin A 0.9g, vitamin K 0.28g, Sodium chloride 1.2g, octyl methoxycinnamate 0.6g, wheat flour are supplied.
A kind of arachidonic microbial fermentation processes, its fermentation medium is by following raw material and its weight portion array Into, per 100g culture mediums in contain:Maltose 12g, beef extract-peptone 47g, dusty yeast 14g, sodium nitrate 2g, potassium chloride 1g, 12 hydrated sulfuric acid hydrogen potassium 0.6g, vitamin B120.37g, vitamin K 0.19g, sodium acid carbonate 1.8g, water are supplied.
A kind of specific steps of arachidonic microbial fermentation processes, it is as described below:
(1)Seed culture is expected in the common Mortierella fermentation of producing arachidonic acid admittedly
(ⅰ)Actication of culture:Activated using slant strains, test tube slant culture medium is PDA solid mediums, by producing arachidonic acid Common Mortierella strain be connected to PDA inclined-planes, 24-26 DEG C is cultivated 2-3 days.
(ⅱ)Admittedly expect the preparation of seed culture medium:Above-mentioned solid medium dispensing is mixed in proportion, 80-100 DEG C of boiling 20-30min, dries to not conglomeration of scattering, and is dispensed into specification as in KShi bottles of 1000mL, 121 DEG C sterilize by 200g/ bottles 30min。
(ⅲ)Admittedly expect the culture of seed:Fresh slant strains are added into spore under the aseptic washings of 15-25mL, spore is made and is hanged Liquid, pours into the solid material culture medium that sterilized, and jog makes its mixing of trying one's best, and is cultivated 2-3 days in 24-26 DEG C, respectively at 12h and 24h Respectively shake up once, as the parent species of one grade fermemtation.
(2)Fermented and cultured
(ⅰ)The preparation of fermentation medium, it is 5.8-6.0,121 DEG C of sterilizings that above-mentioned fermentation medium each component is mixed into regulation pH 30min。
(ⅱ)Shake flask fermentation culture, i.e. sample fermented and cultured
With the above-mentioned spore for expecting the surface of the seed admittedly under the aseptic washings of 200-300ml, spore suspension is made, is 5- by percent by volume 10% inoculum concentration accesses Medium of shaking flask fermentation, and cultivation temperature is 26-30 DEG C, and shaking speed 150-200r/min is cultivated 3-5 days; Wet thallus are collected after fermentation ends, the grease extracted after drying in dry mycelium carries out gas chromatographic detection, detects arachidonic acid Recovery rate.
(ⅲ)Ferment tank culture, i.e., middle sample fermented and cultured:With above-mentioned solid material kind sublist under the aseptic washings of 200-300ml The spore in face, is made spore suspension, is that 5-10% inoculum concentrations access one grade fermemtation tank by percent by volume, and fermentation temperature is 26-30 DEG C, cultivate 1.5-2.5 days;One grade fermemtation to the inoculum concentration percent by volume of second order fermentation is 10-20%, fermentation temperature early stage control System promotes thalli growth at 26-30 DEG C, and temperature, to promote arachidonic acid oil synthesis, is adjusted downward to 18-20 DEG C, training by the later stage The cycle of supporting is 3-4.5 days;The need for ensure thalli growth and Synthetic Oil, whole fermentation process is except auto-feeding is through 118 DEG C The percentage by weight of sterilizing 25min is 40% glucose solution, and percentage by weight is that 28% ammoniacal liquor is used to control reduced sugar to exist Preceding 40h is added auxiliary to be that 3-8g/L and pH is outside 5.8-6.0, to be additionally carried out 2 times and add auxiliary material manually after 6-8g/L, 40h The material time is respectively fermentation 36h and 69h, and auxiliary material is respectively by glucose, soybean-cake flour, corn starch, olive oil, dipotassium hydrogen phosphate And all kinds of trace element compositions, trace element can be vitamin B1, vitamin B2, vitamin B6, vitamin B12, nicotinic acid, cigarette The combination of one or more in acid amide, calcium pantothenate, folic acid, biotin, chlorophyll;Wet thallus are collected after fermentation ends, is dried The grease extracted afterwards in dry mycelium carries out gas chromatographic detection, detects arachidonic acid recovery rate.
Described above not limitation of the present invention, the present invention is also not limited to the example above.The art it is common In essential scope of the invention, change, remodeling, addition or the replacement made should also belong to protection of the invention to technical staff Scope.

Claims (5)

1. a kind of arachidonic microbial fermentation processes, it is characterised in that solid medium is made up of following raw material:Beef Cream peptone, dusty yeast, maltose, vitamin A, vitamin K, sodium chloride, octyl methoxycinnamate, wheat flour.
2. a kind of arachidonic microbial fermentation processes according to claim 1, it is characterised in that solid medium It is made up of following raw material and its parts by weight, is contained in every 100g culture mediums:Beef extract-peptone 30-50g, dusty yeast 5-10g, Maltose 20-25g, vitamin A 0.5-1g, vitamin K 0.25-0.5g, sodium chloride 1.2g, octyl methoxycinnamate 0.5- 0.8g, wheat flour are supplied.
3. a kind of arachidonic microbial fermentation processes according to claim 1, it is characterised in that fermentation medium It is made up of following raw material:Maltose, beef extract-peptone, dusty yeast, sodium nitrate, potassium chloride, 12 hydrated sulfuric acid hydrogen potassium, dimension life Plain B12, vitamin K, sodium acid carbonate, water.
4. a kind of arachidonic microbial fermentation processes according to claim 3, it is characterised in that fermentation medium It is made up of following raw material and its parts by weight, is contained in every 100g culture mediums:Maltose 10-15g, beef extract-peptone 30- 50g, dusty yeast 10-15g, sodium nitrate 1-3g, potassium chloride 1-2g, 12 hydrated sulfuric acid hydrogen potassium 0.5-1g, vitamin B120.25- 0.5g, vitamin K 0.1-0.2g, sodium acid carbonate 1-2g, water are supplied.
5. a kind of arachidonic microbial fermentation processes according to claim 1, it is characterised in that specific steps, such as It is lower described:
1)Seed culture is expected in the common Mortierella fermentation of producing arachidonic acid admittedly
ⅰ)Actication of culture:Activated using slant strains, test tube slant culture medium is PDA solid mediums, by producing arachidonic acid Common Mortierella strain be connected to PDA inclined-planes, 24-26 DEG C is cultivated 2-3 days.
ⅱ)Admittedly expect the preparation of seed culture medium:Above-mentioned solid medium dispensing is mixed in proportion, 80-100 DEG C of boiling 20- 30min, dries to not conglomeration of scattering, and is dispensed into KShi bottles that specification is 1000mL by 200g/ bottles, 121 DEG C of sterilizing 30min.
ⅲ)Admittedly expect the culture of seed:Fresh slant strains are added into spore under the aseptic washings of 15-25mL, spore suspension is made, poured into Sterilized solid material culture medium, and jog makes its mixing of trying one's best, and is cultivated 2-3 days in 24-26 DEG C, and one is respectively shaken up respectively at 12h and 24h It is secondary, as the parent species of one grade fermemtation.
2)Fermented and cultured
ⅰ)The preparation of fermentation medium, it is 5.8-6.0,121 DEG C of sterilizings that above-mentioned fermentation medium each component is mixed into regulation pH 30min。
ⅱ)Shake flask fermentation culture, i.e. sample fermented and cultured
With the above-mentioned spore for expecting the surface of the seed admittedly under the aseptic washings of 200-300ml, spore suspension is made, is 5- by percent by volume 10% inoculum concentration accesses Medium of shaking flask fermentation, and cultivation temperature is 26-30 DEG C, and shaking speed 150-200r/min is cultivated 3-5 days; Wet thallus are collected after fermentation ends, the grease extracted after drying in dry mycelium carries out gas chromatographic detection, detects arachidonic acid Recovery rate.
ⅲ)Ferment tank culture, i.e., middle sample fermented and cultured:With the above-mentioned the surface of the seed of material admittedly under the aseptic washings of 200-300ml Spore, is made spore suspension, is that 5-10% inoculum concentrations access one grade fermemtation tank by percent by volume, and fermentation temperature is 26-30 DEG C, Culture 1.5-2.5 days;One grade fermemtation to the inoculum concentration percent by volume of second order fermentation is 10-20%, and fermentation temperature beforehand control exists 26-30 DEG C, promote thalli growth, temperature, to promote arachidonic acid oil synthesis, is adjusted downward to 18-20 DEG C, culture week by the later stage Phase is 3-4.5 days;The need for ensure thalli growth and Synthetic Oil, whole fermentation process is except auto-feeding is through 118 DEG C of sterilizings The percentage by weight of 25min is 40% glucose solution, and percentage by weight is that 28% ammoniacal liquor is used to control reduced sugar in preceding 40h For after 6-8g/L, 40h for 3-8g/L and pH be 5.8-6.0 outside, be additionally carried out 2 times and add auxiliary material manually, when adding auxiliary material Between be respectively fermentation 36h and 69h, auxiliary material is respectively by glucose, soybean-cake flour, corn starch, olive oil, dipotassium hydrogen phosphate and each Class trace element composition, trace element can be vitamin B1, vitamin B2, vitamin B6, vitamin B12, nicotinic acid, nicotinic acid The combination of one or more in amine, calcium pantothenate, folic acid, biotin, chlorophyll;Wet thallus are collected after fermentation ends, after drying Extracting the grease in dry mycelium carries out gas chromatographic detection, detects arachidonic acid recovery rate.
CN201611268294.1A 2016-12-31 2016-12-31 A kind of arachidonic microbial fermentation processes Withdrawn CN106834137A (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102373244A (en) * 2011-11-30 2012-03-14 厦门金达威集团股份有限公司 Microorganism fermentation method for arachidonic acid
CN104531787A (en) * 2013-09-13 2015-04-22 厦门大学 Method for preparing arachidonic acid (ARA)

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102373244A (en) * 2011-11-30 2012-03-14 厦门金达威集团股份有限公司 Microorganism fermentation method for arachidonic acid
CN104531787A (en) * 2013-09-13 2015-04-22 厦门大学 Method for preparing arachidonic acid (ARA)

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