CN105734105A - Method for promoting conversion of plant sterols into 9 alpha-hydroxyandrostenedione by Mycobacterium fortuitum - Google Patents
Method for promoting conversion of plant sterols into 9 alpha-hydroxyandrostenedione by Mycobacterium fortuitum Download PDFInfo
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Abstract
The invention relates to a method for converting plant sterols into 9 alpha-hydroxyandrostenedione by using a Mycobacterium fortuitum ATCC 35855 bacterial strain. Especially the method uses ultrasonic wave vibration.
Description
Invention field
The present invention relates to a kind of method that plant sterol is converted into 9 Alpha-hydroxy androstenedione by the MycobacteriumfortuitumATCC35855 of use strain, method particularly employs ultrasonic wave concussion.
Background technology:
AD (androst-4-ene-3,17-dione are called for short: androstenedione or AD) is the steroid hormone irreplaceable intermediate of class medicine, and body plays very important adjustment effect.It may be said that nearly all steroid hormone medicine all produces using AD as initiation material.As for productivity hormone, progestogen, protein anabolic hormone and 17-hydroxy-11-dehydrocorticosterone, can be used for again synthesizing hydrogenated cortisone, oxidation prednisone, medicine planted by Progesterone, estrenol, dexamethasone etc. more than 100, is also the requisite base stock being directly used in and producing contragestive agent mifepristone and all kinds of family planning medication.Nowadays AD constantly is used for developing and produce the main product of new medicine by some developed countries, such as Formestane (Formestane or Lentaron), Deng and steroids immunizing antigen etc., in current worldwide, the application of AD is widened day by day, and the medical kind making raw material production of AD is continuously increased.
Owing to chemical complete synthesis androstenedione is relatively costly, lot of domestic and international scientist studies how to obtain androstenedione by biofermentation method always.The fifties, Upjohn company of the U.S. is that raw material production goes out androstane-4-alkene-3 first with having the soyasterol of double-strand and ergosterol on side chain, 17 diketone (AD) and Androsta-1,4-diene-3,17-dione (ADD) the raw material in this, as synthesizing steroid medicine.In recent years, owing to steroid drugs application quantity increases year by year, the sight of people forwards again the cholesterol that content is more in animals and plants circle, sitosterol, campesterol etc. to, and is considered as the initiation material of the steroid hormone class medicine with tremendous potential.Middle 1960s, first found that some microorganism can be excised the saturated side chains of sterol and obtain AD and ADD by degradation selectivity by Sih etc., the beginning of the seventies, Japan have horse open utilize microbial degradation cholesterol produce ADD succeed, be subject to the great attention of many drugmakers.In order to produce steroid hormone in a large number, researcher attempts to use sterol to be sole carbon source separate microorganism and change the substrate that sterol structure is used as to ferment, and the recovery rate of steroid is improved with the chemical addition agent that can prevent sterol core from degrading, this effort is own obtains remarkable progress (Marsheck etc., ApliedMicroobiology, 23 (1): 72～77,1972).Additionally, Egyptian country research center biological with natural product chemistry system and the research such as Sallam find, utilize phosphate buffer adjustment substrate cultivation base pH value 5.5～7.38 can improve the conversion ratio of biodegradation AD, ADD.Upjohn company is in U.S. Patent No. 4,293, described in 644, a kind of mutant by mycobacteria (ATCC29472) obtains the hero-4-alkene-3 with high yield from multiple types sterin, 17-diketone (AD) is main, and have a small amount of hero-1,4-diene-3, the method for the product of l7-diketone (ADD).Later research finds arthrobacterium, and the microorganism such as Nocard's bacillus and mycobacteria is used equally to directly excise the saturated side chains of sterol, obtains AD and ADD under certain condition, and this makes microbial transformation industrialized production be possibly realized.
Prepare on the basis of AD and ADD at biological fermentation process, have been found that employing fermentation method can prepare 17-hydroxy-11-dehydrocorticosterone with 9 α-OH-AD more easily for raw material in recent years.
Structure activity relationship according to 17-hydroxy-11-dehydrocorticosterone, 11 of steroid hormone have β hydroxyl just can have more powerful drug effect, according to the common technique introducing 11 β hydroxyls at present, it is necessary to introduce α hydroxyl at 9 or 11, be just easy to by being chemically incorporated into 11 β hydroxyls.Prepare corticosteroid drug then need fermentation again to obtain 9 or 11 products for α hydroxyl so androstenedione is raw material.9 Alpha-hydroxy androstenedione (androstane-9 alpha-hydroxy-4-ene-3,17-diketone) have-OH substituent group 9 of cyclopentanoperhydro-phenanthrene, are easy to by being chemically incorporated into 11 β hydroxyls compared with androstenedione, and 11 have β hydroxyl and just can have more powerful drug effect.So two-step fermentation will be carried out from plant sterol, and if 9 Alpha-hydroxy androstenedione can be obtained for raw material by a step of fermenting with plant sterol, then substantial amounts of human and material resources, more enough more effective raising work efficiencies can be saved.
At present, it is primarily present two approach and obtains 9 α-OH-AD.One, two-step fermentation, namely first via mycobacteria to sterol (sitosterol, cholesterol) the disconnected side chain of fermentation, produce AD；nullAD is carried out 9 'alpha '-hydroxylations by microorganism (such as promise Ka Shi or Rhod) again that re-use other，Such as Wei Changlong et al. (NocardiacanicruriaBF313 catalysis steroidal 9 'alpha '-hydroxylation fermentation technology optimization，Food industry science and technology，18 phases in 2014，320 pages) report with androstenedione for raw material，Using NocardiacanicruriaBF313 as experimental strain，Have studied the fermentation technology with androstenedione for raw material Biological preparation 9 Alpha-hydroxies-androstenedione，Investigate conversion medium component、Feeding mode、The factors such as initial pH，Adjusting PH before sterilizing is 7.0，Inoculum concentration with 4% is inoculated，Preculture added substrate intending crystallization mode after 16 hours，Through the conversion of 48 hours，It is in 10g/L situation at feed concentrations，Substrate conversion efficiency may be up to 97.2%，In feed concentrations 20g/L situation，Substrate conversion efficiency is also up to 87.2%.Its two, utilize microorganism one-step method direct fermentation sterol, productive target product 9 α-OH-AD.The spherical protoplast of such as Mycobacterium parental plant, after mutagenic treatment, selects a plant mutant strain M.roseum, and this mutant is different from known sterol degradation mycobacteria on systematics, can be produced 9-OH-AD by sterol high vigor.Usual bacterial strain, under the background of disappearance 3-ketone steroidal-1 (2)-dehydrogenase, is only possible to and accumulates 9-OH-AD as main metabolites.Mycobacteria B-8119 and M.vccae thereafter all confirms that mycobacteria exists two kinds of distinct enzymes in sterol converts and 3,17-diketone steroidal 1 (2)-dehydrogenations are relevant, and the difference of both of which is in that the specificity to AD and 9-OH-AD.The reports such as Russia Donova are produced the research of 9-OH-AD mycobacteria mutant strain by sitosterol.In this work, author applies the selection pressure of stigmasterol, and in conjunction with the reasonable combination of classic mutagenesis effect, can convert stigmasterol with acquisition becomes the bacterial strain of 9-OH-AD.The parent strain mycobacteria sp.Ac-1815D mutagenic and breeding process used is as follows: on agar culture medium, 6/2 strain growth grows into different types of bacterium colony during cultivating.In sitosterol culture medium after 6/2 bacterial strain subculture grown cultures 10 times, it is separated to S-type bacterium colony.The best bacterium colony obtained produces 9-OH-AD (being denoted as 6/2S).
What biofermentation method research was more in addition is strain, but ferment effect is except closely related with strain itself, and the method that strain uses during the fermentation is also particularly significant.Yang Ying points out that in article (microbial degradation sterol side chain converts androstane-4-alkene-3, the progress of 17-diketone, microbiology is circulated a notice of, 2006 33 (6), 142-145) sterol substrates poor solubility and there is the problem that serious product (substrate) suppresses and perplexed the industry of whole steroid class always in aqueous solution culture medium, sterol is a kind of hydrophobic compound, in water, dissolubility is extremely low, this results in substrate and can not well contact with microbial cell, makes conversion ratio on the low side and transformation time extends.Although adopting ultrasonication, surfactant and organic solvent to dissolve substrate achieve certain achievement, but the activity of cell being had certain suppressing thus constraining its application by surfactant and organic solvent.
Utilize Mycobacteriumfortuitum (mycobacterium) strain fermentation to obtain 9 Alpha-hydroxy androstenedione with plant sterol for raw material simultaneously, time is longer, often up to 72 hours, and lengthy fermentation has a problem in that it is first easily cause microorganism too to ferment, the product obtained is converted into 9 Alpha-hydroxy testosterones even degraded by cyclopentanoperhydro-phenanthrene, next to that response time long meeting makes miscellaneous bacteria increase, and the conversion specificity cultivating bacterium declines, thus increasing impurity, 3rd long-time reaction also can cause the production cycle, manufacturing cost, costs of labor etc. rise, it is unfavorable for industrialization.
So how shorten fermentation time and just become another problem needing to solve.
Summary of the invention:
The invention provides a kind of is that substrate prepares 9 Alpha-hydroxies-androstane-4 alkene-3 by phytosterol compositions, 17 diketone (9 Alpha-hydroxy androstenedione, 9 α-OH-AD) method, phytosterol compositions is added at the reactor branching off bacillus spp. microorganism, regulate pH value more than 7, ferment between 20-37 DEG C, phytosterol compositions is made to be changed into 9 α-OH-AD, can promote that plant sterol converts by ultrasonic wave concussion during the fermentation, transformation time shortens more than 1/3, and also androstane-4 alkene-3, the conversion ratio of 17 diketone can be improved.
A kind of is that substrate prepares 9 Alpha-hydroxies-androstane-4 alkene-3, the method for 17 diketone, it is characterised in that ferment between 20-37 DEG C by MycobacteriumfortuitumATCC35855 by phytosterol compositions, and uses ultrasonic wave concussion.
Above-mentioned preparation method, it is characterised in that phytosterol compositions concentration in fermentation liquid is 10-100g/L.
Above-mentioned preparation method, it is characterised in that phytosterol compositions concentration in fermentation liquid is 20-70g/L.
Above-mentioned preparation method, it is characterised in that phytosterol compositions concentration in fermentation liquid is 60-100g/L.
Above-mentioned preparation method, it is characterised in that ultrasonic wave concussion frequency is 25-100KHz.
Above-mentioned preparation method, it is characterised in that ultrasonic wave concussion frequency is 40KHz-100KHz.
Above-mentioned preparation method, it is characterised in that ultrasonic wave concussion frequency is 50KHz-70KHz.
Above-mentioned preparation method, it is characterised in that fermentation culture stage carries out ultrasonic wave concussion before terminating.
Above-mentioned preparation method, it is characterised in that fermentation culture stage carries out ultrasonic wave concussion before proceeding to half.
Above-mentioned preparation method, it is characterised in that seed growth phase complete the post-fermentation and culture stage start before carry out ultrasonic wave concussion.
Above-mentioned preparation method, it is characterised in that seed growth phase complete the post-fermentation and culture stage start before carry out ultrasonic wave concussion and fermentation culture stage start after proceed to half to fermentation culture stage before carry out ultrasonic wave concussion.
Above-mentioned preparation method, it is characterised in that fermentation temperature is 20-30 DEG C.
Above-mentioned preparation method, it is characterised in that the fermentation reaction time is 10-60 hour.
Above-mentioned preparation method, it is characterised in that in sweat, PH is between 7.0-9.
Above-mentioned preparation method, it is characterised in that culture medium contains one or more in agar, carbon source, nitrogenous source, PH regulator, enzyme inducer, enzyme accelerator, water.
Above-mentioned preparation method, it is characterised in that reactor adds emulsifying agent before adding phytosterol compositions.
Above-mentioned preparation method, it is characterised in that reactor adds emulsifying agent before adding phytosterol compositions, and emulsifying agent is one or more in synthetic emulsifier, plant oil emulsifying agent.Above-mentioned preparation method, it is characterised in that synthetic emulsifier is one or more in the emulsifying agent of the fatty acid ester of polyglycols, ethyleneoxy additive compound or commodity Tegin, Tween and Span by name.Above-mentioned preparation method, it is characterised in that plant oil emulsifying agent is one or more in Oleum Helianthi, Semen Maydis oil, Oleum Arachidis hypogaeae semen, soybean oil, Oleum Gossypii semen.
Described phytosterol compositions is from the by-product of processing vegetable oil, and described vegetable oil is selected from one or more in soybean oil, Oleum Brassicae campestris, Semen Maydis oil, Oleum Gossypii semen, Oleum Helianthi, olive oil, Semen Lini oil, Testa oryzae oil.
Described phytosterol compositions is the mixture of vegetable oil and phytosterol compositions, and described vegetable oil is from one or more in soybean oil, Oleum Brassicae campestris, Semen Maydis oil, Oleum Gossypii semen, Oleum Helianthi, olive oil, Semen Lini oil, Testa oryzae oil.Preferred soybean oil.
We have found that by studying, add and cultivate bacterium by after ultrasonic wave concussion, phytosterol compositions is converted into the speed of 9-OH-AD and is significantly improved by microorganism, more surprisingly conversion ratio is significantly improved, so that the purity of 9-OH-AD product, yield are all significantly improved.
Above-mentioned experimental result occurs being likely due to following: be first carry out ultrasonic wave concussion during the fermentation, the collision probability cultivating bacterium, plant sterol, fermentation liquid can be increased, but the cell wall cultivating bacterium has been decomposed, reduce plant sterol and enter endobacillary difficulty, it is possible to improve the speed of fermentation.But surprisingly seed growth phase complete the post-fermentation and culture stage start before carry out ultrasonic wave concussion, the purity of 9-OH-AD, yield can will be made all to be significantly improved, and passing data carries out ultrasonic wave concussion in fermentation culture often, it is only capable of the effect producing to accelerate the speed of fermentation.
Further detail below helps those skilled in the art to implement the present invention.But, this describes in detail and is not construed as the excessive restriction to the scope of the invention.Embodiment discussed herein can be modified and be varied without departing from the spirit of the scope of the invention by those of ordinary skill in the art.
Bacterial fermentation is cultivated and can be divided into Spore cultivation, seed culture, three processes of fermentation culture by its purposes, but these three process can complete in same reactor again, it is also possible to completing in different reactors, even three processes can merge.
Spore cultivation is the process for culture propagation spore, is to make thalline mushroom out, and produces the spore of more high-quality, and requires not easily to cause strain to morph.So to the basic requirement of Spore cultivation base being: first, nutrition not too abundant (particularly organic nitrogen source), otherwise not easily produces spore.As Lycoperdon polymorphum Vitt strepto-can grow well and produce spore in the culture medium of glucose-nitrate-other salt, if but after adding 0.5% yeast extract or casein, just only long mycelia and not long spore.Second, the concentration of inorganic salt used wants appropriate, not so also can affect spore amount and spore color.3rd, it should be noted that the pH of Spore cultivation base and humidity.Spore cultivation base conventional in production has: bran mass, Semen setariae culture medium, rice medium, Semen Maydis chip culture medium and the agar slant culture-medium being configured to glucose, peptone, Carnis Bovis seu Bubali cream and Sal etc..Rice and Semen setariae are commonly used for mycotic spore culture medium, because they nitrogen contents are few, loose, surface area big, so being better Spore cultivation base.The moisture of rice medium need to control at 21%-50%, and bent room air humidity need to control at 90%-100%.Such culture medium general mainly carries out strain in laboratory and goes down to posterity use, is not involved in industrial fermentation process.
Seed culture is for spore-germination, growth and amount reproduction mycelium, and makes thalline look sturdy, becomes for the purpose of energetic " seed ".So the nutritional labeling of seed culture medium requires relatively abundanter and complete, the content of nitrogenous source and vitamin also wants height, but total concentration is slightly thin as well, so can reach higher dissolved oxygen, for the breeding of a large amount of thalli growths.The composition of seed culture medium to consider maintain stable pH in microbial metabolism, and its composition also to be determined according to the physiological feature of different strain.General seed culture medium all uses nutritious and natural organic nitrogen source completely, because some aminoacid can stimulate spore-germination.But inorganic nitrogen-sourced easy utilization, is conducive to thalline to mushroom out, so often including organic and inorganic nitrogen-sourced in seed culture medium.The composition of seed culture medium is preferably closer to fermentation medium, seed so can be made to adapt to rapidly after entering fermentation medium, fast-growth.
Fermentation culture is the process for growth, breeding and synthetic product.It can mushroom out after should making seed inoculation, reaches certain mycelial concentration, makes the thalline grown to synthesize rapidly again and need product.Therefore, the composition of fermentation medium, except having element necessary to thalli growth and except compound, also to have the element-specific needed for product, precursor and accelerator etc..If but the concentration of the total carbon source needed because of growth and biosynthetic products, nitrogenous source, phosphorus source etc. is too high, or when the optimum condition that respectively needs of growth and synthesis two benches requires difference, then it is contemplated that culture medium batch feeding is met.Fermentation medium can also be called biotransformation medium or microbe conversion culture medium.
It is possible if desired to addition phosphate, magnesium and/or ferrous ion are as somatomedin；Also can add buffer to guarantee to be grown in basic neutral pH.During beginning, defoamer is probably useful.When for induction fermentation be the microorganism of the cell or enzyme that separate rather than complete and growth time, it is not necessary to the existence of nutrient substance；But no matter being which kind of situation, culture medium is usually mainly moisture.
nullTerm " plant sterol " includes all of sterol and not restriction as used herein，Such as: sitosterol，Lay oil sterol，Stigmasterol，Brassicasterol (includes dihydro brassicasterol),Desmosterol，chalinosterol，Poriferasterol，Chionasterol，Ergosterol，Coprostenol，Section's enlightening sterol (codisterol)，Isofucosterol (isorucosterol)，24-ethylidenecholest-5-en-3.beta.-ol.，Paulownia sterol，Neural sterol (nervisterol),Lathosterol，Asteriasterol，Chondrillasterol，chondrillasterol，peposterol，Avenasterol，Different avenasterol，fecosterol，Pollinastasterol，Cholesterol and their all naturally occurring or synthetic form and derivant，Including isomer. and include the hydrogenation homologue (" phytostanol (Phytostanols) ") of all of which.Phytostanol includes all saturated or plant sterol that is that hydrogenate and their all naturally occurring or synthetic form and derivant, including isomer.When there is query in description full text, it needs to be understood that term " plant sterol " can comprise plant sterol and phytostanol.
Sterol and stanol (stanols) for bioconversion of the present invention can pass through many kinds of natural origins and obtain.Such as, they can obtain from the processing of vegetable oil (including water plant), described vegetable oil such as Semen Maydis oil and other vegetable oil, wheat germ oil, soybean extract, rice extract, Testa oryzae, Oleum Brassicae campestris, Oleum Helianthi, Oleum sesami.They can also derived from fungus, for instance ergosterol.Therefore, the present invention is not limited to any one source of sterol. and disclosed in United States Patent (USP) 4,420,427, use solvent such as methanol prepares sterol from vegetable oil residue.Or, plant sterol and phytostanol can come from forestry processed side product tall oil pitch (talloilpitch) or slurrying soap (pulpingsoap), as described in United States Patent (USP) 5,770,749, are hereby incorporated by.
Sweat in the present invention, it is possible to that be dissolved in suitable solvent or emulsifying form substrate (phytosterol compositions) and culture of microorganism are added in bioreactor together.Carrying out fermentation until reaching maximum substrate and converting, namely plant sterol is converted into 9-OH-AD.
As long as can promote that phytosterol substrate mixes in a solvent, thus the utilization rate that optimization culture of microorganism is to substrate, it is possible to use any emulsifying agent.Such as include but are not limited to: the fatty acid ester of polyglycols or the emulsifying agent of ethyleneoxy additive compound and commodity Tegin, Tween and Span by name.
Or, it is possible to use solubilizing agent phytosterol compositions is to form settled solution, thus providing contact good with microorganism used therefor in bioconversion.Selected suitable solubilizing agent includes glycol (glycol) class and type siloxane solubilizing agent, and they can make the plant sterol of high concentration be dissolved in Nutrient medium.This will make itself and microorganism good contact, reduce fermentation time, and obtain the relatively high yield of end product.Preferably in itself previously known solubilizing agent is Oleum Helianthi, soybean oil such as.
Fermentation medium preferably comprises the seed culture medium of glucose.
Above-mentioned all culture medium can add phosphate, magnesium and/or ferrous ion, buffer, therein one or more.
Above-mentioned all culture medium, its every liter culture medium contains Semen Maydis pulp 5-50ml.
Above-mentioned culture medium, its every liter culture medium contains inorganic salt 4-10g.
Above-mentioned all culture medium, its every liter fermentation medium contains glucose 5-15g.
Above-mentioned all culture medium, its every liter culture medium contains Semen Maydis pulp 5-50ml, inorganic salt 4-10g, glucose 5-15g.
Above-mentioned culture medium seed culture medium in this way, then contain glucose；Above-mentioned culture medium fermentation medium in this way, then can without glucose.
In fermentation process, it is preferable that temperature maintains in the scope of about 20-37 DEG C, more preferably 25-35 DEG C.Fermentation or conversion process, once complete, namely reclaim 9-OH-AD by known in the art and conventional method.
Detailed description of the invention
Below example represents laboratory test. but, each the extension of known industrial technology can be used to implement the present invention for plant-scale application.
The ATCC mentioned in strain in below example is the abbreviation of Unite States Standard strain collections, and this center is one of international Spawn preservation organization.
Plant sterol in following embodiment is the product more than 95% of the content commercially.
Embodiment 1-3
Strain: MycobacteriumfortuitumATCC35855.
The Semen Maydis pulp taking 10 different lot numbers ferments respectively according to the quantity in the present embodiment and technique.Except Semen Maydis pulp, other material is same batch materials.
Seed growth phase:
Seed culture medium (every liter):
Cultivate base unit weight: 200ml/ flask
Inoculum amount: every new culture medium inoculated of 200m1 is from the 3ml cell suspension of agar slant
Container: 1000ml conical flask
Stirring: agitator (1 " throw) 200rpm
Temperature: 30 DEG C
Growth time: cultivate for 72 hours
Explaining: if having yellow coloured cell sediment to be formed in bottom, being expressed as good culture biological
Method:
Prepare the inoculum for bioconversion in the medium.From agar charge level (cultivating teat glass) inoculation conical flask, aseptically inoculate, pipette sterilized water (5mL) to tremble on face to agar. bacterial cultures is scraped gently with pipette tip. then pipette this suspended culture and put in conical flask. on gyrate shaker, carry out bacterial multiplication (200rpm, l " throw, 30 degree).After cultivating 72 hours, namely this inoculum is transferred in bioreactor.It is worthless to inoculum long term storage before inoculation.In operation, it is also possible to carry out two grades or even third stage culture for seed, seed culture is good, when enter fermentation medium after fermentation time can proper extension, to obtain better biological transformation ratio.
Steroidal fermentation medium (every liter):
40ml Semen Maydis pulp
5.2gNaNO3,
0.8gNH4H2PO4
All the other are sterilized water
Substrate: 30.0g plant sterol (3.0%)
Emulsifying agent: Oleum Helianthi, consumption is shown in following table
One day before use, it is necessary to the Semen Maydis pulp of amount and water (100ml) is mixed is incorporated in conical flask sterilizing (121 DEG C continue 20 minutes).
Mixing water (500ml) and nutrient media components (except plant sterol and Oleum Helianthi) in flask or beaker.Adjust the pH value of culture medium to 8.0 with 1MNaOH solution (40g/LNaOH), in media transfer to bioreactor, will be subsequently heated to 60-70 DEG C.
Beaker is weighed plant sterol (30g), add Oleum Helianthi, heating edge stirring mixture, above-mentioned Oleum Helianthi is poured into (60-70 DEG C) in the fluid medium heated in bioreactor, mends sterilized water to 1L, it is not necessary to stirring.
By fermentation tank sterilizing (121 DEG C continue 30 minutes), it is subsequently cooled to 30 DEG C.Use above-mentioned culture medium 3L.
Fermentation tank uses the bioconversion that mycobacteria carries out:
Rustless steel fermentation tank with effectively bottom stirring carries out Biotransformation experiments.The major parameter of fermentation tank used is: fermentation tank cumulative volume 10 liters, working volume 3 liters, and inoculum amount, with 0.4L, ventilation 0.3L/L/min, stirs 300rpm.
The temperature of culture medium in fermentation tank is adjusted to 30 DEG C, aseptically adds inoculum.Whole process carries out at 30 ± 2 DEG C.From then on the stage starts to pH value and the sterility of finally all monitoring this process.Start to monitor substrate (plant sterol) and product 9-OH-AD after 10 hours.In this process, the pH value of biotransformation mixture generally changes in 1pH unit and does not correct.By analyzing in (HPLC) 2 hours when the product 9-OH-AD content in froth bed reaches constant, it is believed that being complete bioconversion, concrete fermentation time is shown in following table.
Applying ultrasonic wave concussion in sweat, the time and the frequency that specifically carry out ultrasonic wave concussion are shown in following table.HPLC measures the ratio of 9-OH-AD and plant sterol.
Fermentation liquid, with 1,2-dichloroethanes extracting, dilutes suitable multiple after concentrating under reduced pressure, 10000r/min is centrifuged off possible insoluble matter, then high pressure liquid chromatography (HPLC) chromatographic column: Alltima (4.6mm (internal diameter) × 250mm) 5 μm.Mobile phase: petroleum ether: ethyl acetate=6:4, flow velocity: 1.0mL/min, temperature: room temperature, detects wavelength: 240nm.
Result is shown in following table: Spore cultivation, seed culture, fermentation culture
Embodiment 4
Method is similar with embodiment 1-3, but throws concentration of substrate and become 4% (plant sterol 40g), and fermentation culture stage Parameters variation is as follows:
Rustless steel fermentation tank with effectively bottom stirring carries out Biotransformation experiments.The major parameter of fermentation tank used is: fermentation tank cumulative volume 10 liters, working volume 3 liters, and inoculum amount, with 0.4L, ventilation 0.5L/L/min, stirs 400rpm.
Experimental result is shown in following table
Embodiment 5
Method is with embodiment 4, but throws concentration of substrate and become 7% (plant sterol 70g),
Proved by above-described embodiment, it is that substrate prepares 9 Alpha-hydroxies-androstane-4 alkene-3 by MycobacteriumfortuitumATCC35855 by phytosterol compositions, 17 diketone, when ultrasonic wave concussion, achieve good effect, its conversion ratio significantly improves, from there through conventional technical method, it is possible to make the yield of product and quality significantly improve.When feeding intake particularly in high concentration, for instance 7%, by 2 ultrasonic wave concussion, its conversion ratio is significantly better than the method not using ultrasonic wave concussion.
Claims (10)
1. one kind is that substrate prepares 9 Alpha-hydroxies-androstane-4 alkene-3, the method for 17 diketone, it is characterised in that ferment between 20-37 DEG C by MycobacteriumfortuitumATCC35855 by phytosterol compositions, and uses ultrasonic wave concussion.
2. preparation method as claimed in claim 1, it is characterised in that phytosterol compositions concentration in fermentation liquid is 10-100g/L.
3. preparation method as claimed in claim 1, it is characterised in that ultrasonic wave concussion frequency is 25-100KHz.
4. preparation method as claimed in claim 1, it is characterised in that fermentation culture stage carries out ultrasonic wave concussion before terminating.
5. preparation method as claimed in claim 1, it is characterised in that fermentation temperature is 20-30 DEG C.
6. preparation method as claimed in claim 1, it is characterised in that the fermentation reaction time is 10-60 hour.
7. preparation method as claimed in claim 1, it is characterised in that in sweat, PH is between 7.0-9.
8. the preparation method described in claim 1, it is characterised in that culture medium contains one or more in agar, carbon source, nitrogenous source, PH regulator, enzyme inducer, enzyme accelerator, water.
9. the preparation method described in claim 1, it is characterised in that reactor adds emulsifying agent before adding phytosterol compositions.
10. the preparation method described in claim 1, it is characterised in that reactor adds emulsifying agent before adding phytosterol compositions, and emulsifying agent is one or more in synthetic emulsifier, plant oil emulsifying agent.
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| CN111349584A (en) * | 2020-03-13 | 2020-06-30 | 广东本科生物工程股份有限公司 | Mycobacterium vaccae and application thereof in preparation of 9 α -hydroxy-20 α -hydroxymethyl-pregn-4-en-3-one |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111349584A (en) * | 2020-03-13 | 2020-06-30 | 广东本科生物工程股份有限公司 | Mycobacterium vaccae and application thereof in preparation of 9 α -hydroxy-20 α -hydroxymethyl-pregn-4-en-3-one |
| CN111349584B (en) * | 2020-03-13 | 2022-09-27 | 广东本科生物工程股份有限公司 | New mycobacterium aureofaciens and application thereof in preparation of 9 alpha-hydroxy-20 alpha-hydroxymethyl-pregn-4-ene-3 ketone |
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