CN1304986A - Process for preparing microbe oil - Google Patents
Process for preparing microbe oil Download PDFInfo
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- CN1304986A CN1304986A CN 00116051 CN00116051A CN1304986A CN 1304986 A CN1304986 A CN 1304986A CN 00116051 CN00116051 CN 00116051 CN 00116051 A CN00116051 A CN 00116051A CN 1304986 A CN1304986 A CN 1304986A
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Abstract
A microbe oil as addiive of healh-care product and food is preapred from Mortierella isabllina AS3.3410 strain through ultraviolet mutragensis twice, composite mutagensis twice by ultraviolet ray and LiCl, fermenting, screening strains, steaming and parching dried mycelia, squeezing, extractinig from mycelia cake with organic solvent (n-hexane), concentrating, heating, feeding in hydrating pot, adding salt solution, heating while stirring, and cooling. Its advantages are low cost and high content of polyunsaturated fatty acid containing octadecpolyenoic acid.
Description
The present invention relates to the oil and fat chemical field, more specifically relate to a kind of preparation method of microbial oil.
From microorganism, obtain grease at present, only be confined to a spot of laboratory manual work stages, with the oil in the dry mycelium of organic solvent extraction.The fermentation of only having arrived of carrying out suitability for industrialized production now obtains the bacterium powder, this stage, oil in the solvent extraction mycelium, because the mycelium oleaginousness is higher, powder is bigger, only with the wherein all greases of solvent oil extraction, the suitability for industrialized production difficulty is bigger, increased the solid-liquid separation difficulty, and organic solvent residue makes also bacterium oil can't reach the hygienic requirements of state food additive, the more uncomfortable dietary supplements that are fit to do.
The preparation method who the purpose of this invention is to provide a kind of microbial oil by mutagenesis, screening mutant strain, has improved the content of thalline oleaginousness and unsaturated fatty acids.
In order to achieve the above object, the present invention takes following technical measures:
The bacterial classification that is used for producing microbial oil of the present invention is to belong to the deep yellow genus mortierella, and it has the higher thalline oleaginousness and the content of polyunsaturated fatty acid.At first the bacterium that sets out has been carried out mutagenesis screening, deep yellow mortierella Mortierella isabllina AS3.3410 strain is through twice mutagenesis of UV-light, next is to add twice complex mutation of LiCl through UV-light, through fermentation test, filter out Mortierella isabllina AS3.3410 mutant strain 5-1-6 strain.This bacterial strain on August 1st, 2000 in China's typical culture collection center preservation, deposit number is CCTCC NO.M200017.This strain is through the dried mycelia of fermentation biomass 49g/L fermented liquid, oil length about 60%, and produce oil 19.7g/L fermented liquid, linolenic acid 6.18%-7.32%, the polyunsaturated fatty acid that contains 18 carbon polyenoic acids accounts for 44% of total fatty acids.About from mycelia, obtaining grease, adopted and squeezed out most of crude oil earlier, crude oil can reach the first-grade edible oil standard after refining.Residual oil in the bacterium cake with the solvent oil extraction, has so just reduced solvent oil consumption and solvent-extracted workload again.This substep obtains the method for microbial oil can carry out suitability for industrialized production.The characteristics higher according to the mycelium oleaginousness take the pre-mode that leaches of pressing to obtain grease; The 3rd be to the exsiccant mycelium through 90～115 ℃, after 25-35 minute steaming is fried, squeezing, can obtain major part have thalline the pre-oil expression fat of intrinsic fragrance, pre-pressed crude oil does not wherein contain organic solvent.The remaining 10% greasy bacterium cake of having an appointment that contains is with organic solvent-normal hexane or the extraction of its isomer.The organic solvent content volume ratio of extraction is 0.6-1: 1, and temperature 45-60 ℃, 30-60 minute; The 4th is concentrated, and the indirect steam of extraction liquid in long-tube evaportor is heated to 80-100 ℃, the open steam 95-120 in the dish formula stripping tower ℃, concentrates and can obtain to leach crude oil; The 5th is that pre-pressed crude oil and leaching crude oil are squeezed into two aquation pots respectively, the salts solution that adds 1/10 volume 1-5%, heated and stirred continues 10-30 minute to 70-90 ℃, leaves standstill cooling 4-24 hour, the crude oil that aquation is good pumps in the precipitation pot respectively, feed 110-150 ℃ of open steam, the atmospheric indirect steam of 3-5, vacuum tightness is-650～-750mmHg, obtain finished product oil, by leach in the oil that the crude oil refining goes out residual molten≤50 * 10
-6, by in the refining oil in the pre-pressed crude oil residual molten be 0.
Embodiment 1
The bacteria suspension 4ml that dilution is prepared moves in the sterile petri dish of 60ml, puts into aseptic magnetic stirring bar, puts on the magnetic stirring apparatus, and 45 " and 60 " are shone at the 30cm place respectively under the 20W ultraviolet lamp, and entire operation is all carried out in Bechtop.
Each 0.5ml of bacteria suspension that gets non-irradiated bacteria suspension (comparing) respectively and shone under lamp carries out dilution in various degree, getting last 3 dilution diluent 0.2ml is applied on the potato culture medium flat plate, with preparing the aseptic rod coating that is coated with, cultivated 3-4 days, and caused mortality ratio more than 90% for 28 ℃.
The bacterial strain that grows transferred shake bottle in the inclined-plane simultaneously, cultivate, microscopic examination is to the stand density and the fat particle of thalline, collect dry mycelium, oven dry, survey biomass, survey oleaginousness, select the better bacterial strain of two strains in view of the above, repeat above-mentioned ultraviolet mutagenesis again, screening, obtained strains is again behind uv irradiating, bacteria suspension, be coated on the potato substratum that is contained in LiCl and cultivate, screening so repeats twice, promptly obtains the prominent bacterial strain 5-1-6 strain of high yield of Mortierellaisabellina AS3.3410 strain, the mutant strain of gained is inoculated on the PDA substratum, cultivated 7 days.
With spore inoculating in the seeding tank that 50L material is housed 40-45 hour, 28 ℃ of temperature all moved in the fermentor tank that the 500L material is housed again, can obtain the dry mycelium of 24.5kg after 72-96 hour, dry mycelium is steamed stir-fry 30 minutes, and after the indirect steam temperature was 105 ℃, squeezing can obtain the 10kg pre-pressed crude oil.
12.5kg the bacterium cake, the solvent that adds 13L soaked 1 hour at 55 ℃, collect extraction liquid, extraction liquid concentrates in the dish formula vapour tower and can obtain 1.5kg leaching crude oil through long-tube evaportor, to leach crude oil and go into 70 ℃ of addings of heating 0.15kg3%NaCl solution in the pump aquation pot, stir cooling in 20 minutes and left standstill 24 hours, skim upper strata oil, pump into precipitation pot vacuum tightness-700mmHg, pass to 130 ℃ of open steams, can get residual solvent at last is 50 * 10
-6Following processed oil 1.45kg.
Pre-pressed crude oil aquation dehydration with leaching the crude oil treating processes, can obtain the processed oil about 11.5kg, and two kinds of oil contents are opened, and the local flavor of pre-pressed crude oil is better.
Embodiment 2
Spore inoculating is cultivated 40-45 hour whole the immigration in the fermentor tank that the 1200L material is housed in the seeding tank that the 120L material is housed, put jar in 72-96 hour and can obtain the 50kg dry mycelium, steam stir-fry 30 minutes for thalline, indirect steam is 105 ℃, and squeezing can obtain the prediction press for extracting juice crude oil of 20.55kg then.
28.4kg the bacterium cake, the solvent oil that adds 28.4L soaked 1 hour at 55 ℃, collect extraction liquid, extraction liquid concentrates through long-tube evaportor, dish formula stripping tower and can obtain 3.32kg and leach crude oil, will leach crude oil and pump in the aquation pot 70 ℃ of heating and add 0.32kg3%NaCl solution, stirs minute to cool off to leave standstill 24 hours, skim upper strata oil, pump into precipitation pot vacuum tightness-700mmHg, pass to 130 ℃ of open steams, can obtain residual solvent at last is 50 * 10
-6Following processed oil 3.18kg.
Pre-oil expression aquation dehydration with going out the crude oil treating processes, can obtain the processed oil of 19.8kg.
Implementation step is identical with embodiment 1.
Embodiment 3
With spore inoculating in the seeding tank that 500L material is housed, cultivate and all moved in 40-45 hour in the fermentor tank that the 2500L material is housed, put in 72-96 hour and jar can obtain the 102kg dry mycelium, dry mycelium is steamed fried 30 minutes, indirect steam is 105 ℃, and squeezing can obtain the prediction press for extracting juice crude oil of 38.8kg then.
The bacterium cake of 62kg, the solvent oil that adds 62L soaked 1 hour at 55 ℃, collect extraction liquid, extraction liquid concentrates through long-tube evaportor, dish formula stripping tower and can obtain 7.1kg and leach crude oil, will leach crude oil and pump into and heat 70 ℃ and add 0.7kg3%NaCl solution in the aquation pot, stirred 20 minutes, left standstill 24 hours, the upper strata oil pump is gone into precipitation pot, vacuum tightness-700mmHg, pass to 130 ℃ of open steams, can obtain residual solvent at last is 50 * 10
-6Following processed oil 6.9kg.
Pre-oil expression aquation dehydration with going out the crude oil treating processes, can obtain the processed oil of 37.2kg.
Implementation step is identical with embodiment 1.
The present invention compared with prior art has the following advantages and effect:
The present invention has found new oil sources for producing polyunsaturated fatty acid, and by methods such as mutagenesis, screenings The oil content of bacterial strain and the content of polyunsaturated fatty acid have been improved. The grease of gained can reach by this method The sanitary standard of state food additive. The present invention utilizes the micro-organisms polyunsaturated fatty acid, together with planting Thing, deep-sea fish produce polyunsaturated fatty acid and compare: simple process, easy to implement the method, its raw material abundance is produced The condition restriction such as climate, environment not, through fermentation biomass 49g dry mycelium zymotic fluid, oil content 60% produces Oil 19.7g/L zymotic fluid, leukotrienes 6.18-7.32%, the polyunsaturated fatty acid that contains 18 carbon polyenoic acids accounts for always 44% of aliphatic acid, cost is low, has reduced the cost of producing polyunsaturated fatty acid, so the microbial grease system of using The nutrient and healthcare products, the food additives that become, its price more can be accepted by popular.
Claims (1)
1, a kind of preparation method of microbial oil is characterized in that at first the bacterium that sets out being carried out mutagenesis screening, and deep yellow mortierella Mortierella isabllina AS3.3410 strain is through twice mutagenesis of UV-light; Next is to add twice complex mutation of LiCL through UV-light, through fermentation, screening bacterial strain Mortierella isabllina AS3.3410 mutant strain 5-1-6 strain, CCTCC NO.M200017; The 3rd is to 90-115 ℃ of exsiccant mycelium process, and after 25-35 minute steaming was fried, squeezing extracted with organic solvent-normal hexane the bacterium cake again, and the organic solvent content volume ratio of extraction is 0.6～1: 1; The 4th is concentrated, and the indirect steam of extraction liquid in long-tube evaportor is heated to 80-100 ℃, the open steam 95-120 in the dish formula stripping tower ℃; The 5th is that pre-pressed crude oil and leaching crude oil are squeezed into the aquation pot, the salts solution that adds 1/10 volume 3%, heated and stirred is to 70-90 ℃, continue 10-30 minute, cooling pumps into crude oil respectively in the precipitation pot again, feeds 110-150 ℃ of open steam, the atmospheric indirect steam of 3-5, vacuum tightness be-650～-750mmHg.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN00116051A CN1109093C (en) | 2000-09-28 | 2000-09-28 | Process for preparing microbe oil |
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| Application Number | Priority Date | Filing Date | Title |
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| CN00116051A CN1109093C (en) | 2000-09-28 | 2000-09-28 | Process for preparing microbe oil |
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| CN1304986A true CN1304986A (en) | 2001-07-25 |
| CN1109093C CN1109093C (en) | 2003-05-21 |
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| CN00116051A Expired - Fee Related CN1109093C (en) | 2000-09-28 | 2000-09-28 | Process for preparing microbe oil |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101108997B (en) * | 2006-07-19 | 2010-07-21 | 中国科学院大连化学物理研究所 | Process for preparing microbe oil |
| EP2239028A1 (en) * | 2001-12-12 | 2010-10-13 | Martek Biosciences Corporation | Extraction and Winterization of Lipids From Oilseed and Microbial Sources |
| CN101338328B (en) * | 2007-07-04 | 2011-04-20 | 中国科学院大连化学物理研究所 | Method for enhancing microbe oil fermentation production efficiency |
| CN101497902B (en) * | 2008-02-03 | 2011-11-09 | 中国科学院大连化学物理研究所 | Process for preparing microbe oil |
| CN102325892A (en) * | 2008-12-01 | 2012-01-18 | 赢泰医药科技发展有限公司 | Utilize slime bacteria to produce omega-3 lipid acid |
| CN102575271A (en) * | 2009-04-14 | 2012-07-11 | 索拉兹米公司 | Methods of microbial oil extraction and separation |
| CN102559790A (en) * | 2012-02-07 | 2012-07-11 | 清华大学 | Method for improving production of microbial oils by fermentation of oil-producing microorganism |
| CN103642580A (en) * | 2013-06-05 | 2014-03-19 | 青岛渤海科技有限公司 | Method for extracting microbial lipid through dry method |
| US9115332B2 (en) | 2009-05-26 | 2015-08-25 | Solazyme, Inc. | Fractionation of oil-bearing microbial biomass |
| US9896642B2 (en) | 2008-10-14 | 2018-02-20 | Corbion Biotech, Inc. | Methods of microbial oil extraction and separation |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW533235B (en) * | 1997-06-11 | 2003-05-21 | Idemitsu Petrochemical Co | Method for extracting fat-soluble components from microbial cells |
-
2000
- 2000-09-28 CN CN00116051A patent/CN1109093C/en not_active Expired - Fee Related
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8480904B2 (en) | 2001-12-12 | 2013-07-09 | Dsm Ip Assets B.V. | Extraction and winterization of lipids from oilseed and microbial sources |
| EP2239028A1 (en) * | 2001-12-12 | 2010-10-13 | Martek Biosciences Corporation | Extraction and Winterization of Lipids From Oilseed and Microbial Sources |
| EP2261312A1 (en) * | 2001-12-12 | 2010-12-15 | Martek Biosciences Corporation | Extraction and Winterization of Lipids from Oilseed and Microbial Sources |
| US8012354B2 (en) | 2001-12-12 | 2011-09-06 | Martek Biosciences Corporation | Extraction and winterization of lipids from oilseed and microbial sources |
| CN101108997B (en) * | 2006-07-19 | 2010-07-21 | 中国科学院大连化学物理研究所 | Process for preparing microbe oil |
| CN101338328B (en) * | 2007-07-04 | 2011-04-20 | 中国科学院大连化学物理研究所 | Method for enhancing microbe oil fermentation production efficiency |
| CN101497902B (en) * | 2008-02-03 | 2011-11-09 | 中国科学院大连化学物理研究所 | Process for preparing microbe oil |
| US11542456B2 (en) | 2008-10-14 | 2023-01-03 | Corbion Biotech, Inc. | Methods of microbial oil extraction and separation |
| US9896642B2 (en) | 2008-10-14 | 2018-02-20 | Corbion Biotech, Inc. | Methods of microbial oil extraction and separation |
| CN102325892B (en) * | 2008-12-01 | 2015-01-14 | 沙尔大学 | Production of omega-3 fatty acids by myxobacteria |
| CN102325892A (en) * | 2008-12-01 | 2012-01-18 | 赢泰医药科技发展有限公司 | Utilize slime bacteria to produce omega-3 lipid acid |
| CN106367198A (en) * | 2009-04-14 | 2017-02-01 | 泰拉瑞亚控股公司 | Methods of microbial oil extraction and separation |
| CN102575271A (en) * | 2009-04-14 | 2012-07-11 | 索拉兹米公司 | Methods of microbial oil extraction and separation |
| US9115332B2 (en) | 2009-05-26 | 2015-08-25 | Solazyme, Inc. | Fractionation of oil-bearing microbial biomass |
| CN102559790B (en) * | 2012-02-07 | 2014-03-12 | 清华大学 | Method for improving production of microbial oils by fermentation of oil-producing microorganism |
| CN102559790A (en) * | 2012-02-07 | 2012-07-11 | 清华大学 | Method for improving production of microbial oils by fermentation of oil-producing microorganism |
| CN103642580A (en) * | 2013-06-05 | 2014-03-19 | 青岛渤海科技有限公司 | Method for extracting microbial lipid through dry method |
| CN103642580B (en) * | 2013-06-05 | 2015-11-25 | 青岛海智源生命科技有限公司 | A kind of dry method extracts the method for microbial oil |
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| CN1109093C (en) | 2003-05-21 |
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