SU1613492A1 - Method of producing lipids - Google Patents
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- SU1613492A1 SU1613492A1 SU884478668A SU4478668A SU1613492A1 SU 1613492 A1 SU1613492 A1 SU 1613492A1 SU 884478668 A SU884478668 A SU 884478668A SU 4478668 A SU4478668 A SU 4478668A SU 1613492 A1 SU1613492 A1 SU 1613492A1
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Abstract
Изобретение относитс к технической микробиологии, в частности к способам получени липидов микробиологическим синтезом. Микробные липиды могут быть использованы в качестве заменителей технических жиров. Цель изобретени - повышение содержани олеиновой кислоты в липидах. Штаммы липогенных микроскопических грибов CUNNING-HAMELLA, JAPONICA ВКМ F - 1204, ASPERGILLUS TERREUS ВКМ F-67, FUSARIUM OXYSPORUM ВКМ F-137 или ALTERNARIA CUCUMORINA ВКМ F-1881 выращивают глубинным способом на питательной среде, содержащей источники углерода, азота, фосфора и стимул тор роста. Соотношение C:N равно 50:1. В качестве источника углерода используют сточные воды производства оливкового масла, содержащие 3,0-3,8% сухих веществ следующего состава, %: редуцирующие вещества 40-50This invention relates to technical microbiology, in particular, to methods for producing lipids by microbiological synthesis. Microbial lipids can be used as substitutes for technical fats. The purpose of the invention is to increase the content of oleic acid in lipids. Strains lipogenic microscopic fungi CUNNING-HAMELLA, JAPONICA VKM F - 1204, ASPERGILLUS TERREUS VKM F-67, FUSARIUM OXYSPORUM VKM F-137 or ALTERNARIA CUCUMORINA VKM F-1881 grown deep method on a nutrient medium containing sources of carbon, nitrogen, phosphorus and incentive growth torus. The C: N ratio is 50: 1. As a carbon source, use is made of olive oil production effluent containing 3.0-3.8% of dry substances of the following composition,%: reducing substances 40-50
пектиновые вещества 16,5-20pectic substances 16,5-20
жиры 7,5-8,0fats 7.5-8.0
клетчатка 0,2fiber 0,2
общий азот 0,2-0,3total nitrogen 0,2-0,3
в т.ч.белковый 0,25-0,27including protein 0,25-0,27
небелковый 0,01-0,015non-protein 0.01-0.015
сырой протеин 1,2-1,8. Содержание РВ в сточных водах 1,5-2,5%. Затем биомассу отдел ют, сушат и экстрагируют из нее липиды. Выход липидов 30-57%. Содержание олеиновой кислоты в липидах 65,6-79,1%. 2 табл.raw protein 1,2-1,8. The RV content in wastewater is 1.5-2.5%. The biomass is then separated, dried and lipids are extracted from it. The output of lipids 30-57%. The content of oleic acid in lipids is 65.6-79.1%. 2 tab.
Description
Изобретение относитс к технической микробиологии и касаетс способа получени липидов . П1кробиологическим синтезом. Микробные липиды могут быть использованы в качестве заменителей технических Ж1гров.This invention relates to technical microbiology and concerns a method for producing lipids. P1krobiologichesky synthesis. Microbial lipids can be used as substitutes for technical Zh1grav.
Цель изобретени - повышение содержани олеиновой кислоты в липидах.The purpose of the invention is to increase the content of oleic acid in lipids.
Способ получени липидов осуществл ют следующим образом.The method for producing lipids is carried out as follows.
Отаммы липигенных микроскопических грибов Cunninghamella japonica ВКМ F-1204, Aspergillus terreus DKM F-67, Fusariun oxysporum BKM F-137Otammy lipigenic microscopic fungi Cunninghamella japonica VKM F-1204, Aspergillus terreus DKM F-67, Fusariun oxysporum BKM F-137
или Alternaria cucumerina BKM F-1881 культивируют глубинным способом на питательной среде, содержащей сточные воды производства оливкового масла (отходы маслоэкстракционных заводов ) в качестве источника углерода. Среда содержит также источник азота и фосфора, предпочтительно в виде фосфата аммони и стимул тор роста, например автолизат дрожжей.or Alternaria cucumerina BKM F-1881 is cultivated in a deep way on a nutrient medium containing the waste water from the production of olive oil (waste from oil extraction plants) as a carbon source. The medium also contains a source of nitrogen and phosphorus, preferably in the form of ammonium phosphate and a growth promoter, such as yeast autolysate.
Сточные воды производства оливкового масла содержат 3,0 - 3,8 сухих BepiecTB (СВ) следующего согтава, %:The wastewater from the production of olive oil contains 3.0 - 3.8 dry BepiecTB (CB) of the following grams,%:
PeflyiwpyKiuifie вещест- ва РВ40 - 50PeflyiwpyKiuifie PB40 - 50
Пектиновые вещества 16,5 - 20 Жиры 7,5 - 8,0Pectic substances 16.5 - 20 Fats 7.5 - 8.0
Клетчатка0,2Cellulose0,2
Общий азот0,2 - 0,3Total nitrogen 0,2 - 0,3
в том числе белковый0 ,25 - 0,27 небелковый0,01 - 0,015 Сырой протеин1,2-1,8 Содержание РВ в сточных водах t,5 - 2,5%. РВ состо т в основном из глюкозы, фруктозы, caxapo3fji, ксилозы и арабинозы.including protein0.0, 25 - 0.27 non-protein0.01 - 0.015 Raw protein1.2-1.8 RV content in wastewater t, 5 - 2.5%. PBs consist mainly of glucose, fructose, caxapo3fji, xylose, and arabinose.
Процесс ведут при соотношении C:N равном 50:1, т.е. в услови х лимити- зации содержани азота в среде. Затем биомассу отдел ют от жидкой фазы , сушат и экстрагируют из нее липпды .The process is conducted at a C: N ratio of 50: 1, i.e. in conditions of limiting the nitrogen content in the medium. Then the biomass is separated from the liquid phase, dried and the lipids are extracted from it.
Пример 1. Штамм микроскопического гриба Cunninghamilla japoni- са ВКМ F-1204 культивируют на питательной среде, содержащей 2,5% (по РВ) сточных вод, 0,1% (NH)2HP04 и 0,05% дрожжевого автолизата. Параллельно провод т выращивание на среде , содержащей 0,15% (NH4)z.MPO.Example 1. The strain of the microscopic fungus Cunninghamilla japonis VKM F-1204 is cultivated on a nutrient medium containing 2.5% (by PB) wastewater, 0.1% (NH) 2HP04 and 0.05% yeast autolysate. In parallel, they are grown on a medium containing 0.15% (NH4) z.MPO.
Среду разливают по 80 мл в колбы емкостью 500 мл, довод т рН до 6,0 и стерилизуют. Затем засевают 7-су- точной культурой, выращенной на сусло-агаровой среде. Процесс выращивани ведут при 26°С в течение 72 ч глубинным способом.The medium is poured into 80 ml flasks with a capacity of 500 ml, adjusted to pH 6.0 and sterilized. Then, they are seeded with 7-day-old culture grown on wort agar medium. The growing process is carried out at 26 ° C for 72 hours in the deepest manner.
Полученную биомассу отдел ют от жидкой фазы, промывают, сушат и экстрагируют хлороформом. Из экстракта липиды вьиел ют нод вакуумом.The resulting biomass is separated from the liquid phase, washed, dried and extracted with chloroform. From the extract, lipids are removed by vacuum.
Состав жирных кислот определ ют методом газовой хроматограции на хроматографе Хром-4.The fatty acid composition is determined by gas chromatography on a Chromo-4 chromatograph.
Полученные результаты приведены в таблице 1, 2.The results are shown in table 1, 2.
Пример 2.В качестве микроорганизма используют штамм Altema- ria cucumerina ВКМ F-1881. Состав питательной среды идентичен примеру 1. C:N 50:1.Example 2. As a microorganism, the strain Altemia cucumerina VKM F-1881 is used. The composition of the nutrient medium is identical to example 1. C: N 50: 1.
Выход биомассы 84% от РВ. Выход липидов 35% от абс. сухой биомассыBiomass yield 84% of PB. The output of lipids 35% of abs. dry biomass
К{ир но кислотный состав липидов, % С«;о .9. C,4:o1,6j С,б;о9,7; С,е ,о 2,3, С 1ft.., 68,7,- ,г 11,6, ЬK {ir no acid composition of lipids,% C "; o .9. C, 4: o1.6j C, b; o9.7; C, e, about 2.3, C 1ft .., 68.7, -, g 11.6, b
Пример 3. Процесс ведут по гфимеру 2, но в качестве микроорга- . низма используют штамм Aspergillus terreus BKIl F-67.Example 3. The process is carried out according to gfimer 2, but as a microorganism. nizm use a strain of Aspergillus terreus BKIl F-67.
Выход биомассы 66,4% от РВ, выход пипидов 30% от абс. сухой биомассы.The biomass yield is 66.4% of PB, the output of pipids is 30% of abs. dry biomass.
)1Сир но кислотный состав липидов, %: С11; о С,,;о 0,81; С(,:0 9,5; .о 2; С ig., 71,6; С 16 , 3 .) 1Cir but acid composition of lipids,%: C11; about With ,,; about 0,81; C (,: 0 9.5; .o 2; C ig., 71.6; C 16, 3.
Пример 4. Процесс ведут по примеру 2, но в качестве микроорганизма используют штамм Fusarium oxys- porum ВКМ F-137.Example 4. The process is carried out according to example 2, but the strain Fusarium oxysporum VKM F-137 is used as a microorganism.
Выход биомассы 66,6% от РВ, выход липидов 32% от абс. сухой биомассы.Biomass yield is 66.6% of PB, lipid yield is 32% of abs. dry biomass.
Жирнокислотный состав липидов, %: CH-,O 0,3; 15,6; 5,3; 0 (в .-( 65,5; Сда 2. 12,2; С д-. 1,4.Fatty acid composition of lipids,%: CH-, O 0.3; 15.6; 5.3; 0 (in .- (65.5; D 2. 2. 12.2; C d-. 1.4.
Как следует из примеров 1 - 4, выход липидов 30 - 57%, содержание олеиновой кислоты 65,5 - 79,1%.As follows from examples 1 to 4, the yield of lipids is 30 to 57%, the content of oleic acid is 65.5 to 79.1%.
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SU884478668A SU1613492A1 (en) | 1988-06-27 | 1988-06-27 | Method of producing lipids |
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Cited By (6)
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RU2468077C2 (en) * | 2011-02-11 | 2012-11-27 | Химический Факультет Московского Государственного Университета Имени М.В. Ломоносова | Method of producing lipids |
US10533155B2 (en) | 2016-03-01 | 2020-01-14 | Sustainable Bioproducts, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US10851396B2 (en) | 2014-07-03 | 2020-12-01 | The Fynder Group, Inc. | Acidophilic fusarium oxysporum strains, methods of their production and methods of their use |
US11039635B2 (en) | 2019-02-27 | 2021-06-22 | The Fynder Group, Inc. | Food materials comprising filamentous fungal particles |
US11118305B2 (en) | 2019-06-18 | 2021-09-14 | The Fynder Group, Inc. | Fungal textile materials and leather analogs |
US11297866B2 (en) | 2017-08-30 | 2022-04-12 | The Fynder Group, Inc. | Bioreactor system for the cultivation of filamentous fungal biomass |
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1988
- 1988-06-27 SU SU884478668A patent/SU1613492A1/en active
Non-Patent Citations (1)
Title |
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Авторско З свидетельство СССР К 270663, кл. С 12 Р 7/64, 1969. Авторское свидетельство СССР , № 1050295, 1ш. С 12 Р 7/64, 1981. * |
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RU2468077C2 (en) * | 2011-02-11 | 2012-11-27 | Химический Факультет Московского Государственного Университета Имени М.В. Ломоносова | Method of producing lipids |
US10851396B2 (en) | 2014-07-03 | 2020-12-01 | The Fynder Group, Inc. | Acidophilic fusarium oxysporum strains, methods of their production and methods of their use |
RU2742437C2 (en) * | 2014-07-03 | 2021-02-05 | Де Файндер Груп, Инк. | Acidophilic strains fusarium oxysporum, methods for producing and methods for the use thereof |
US11015168B2 (en) | 2016-03-01 | 2021-05-25 | The Fynder Group, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US10533155B2 (en) | 2016-03-01 | 2020-01-14 | Sustainable Bioproducts, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US10590379B2 (en) | 2016-03-01 | 2020-03-17 | Sustainable Bioproducts, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US10577579B2 (en) | 2016-03-01 | 2020-03-03 | Sustainable Bioproducts, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US11001801B2 (en) | 2016-03-01 | 2021-05-11 | The Fynder Group, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US11505779B2 (en) | 2016-03-01 | 2022-11-22 | The Fynder Group, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US11261420B2 (en) | 2016-03-01 | 2022-03-01 | The Fynder Group, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
US10787638B2 (en) | 2016-03-01 | 2020-09-29 | The Fynder Group, Inc. | Filamentous fungal biomats, methods of their production and methods of their use |
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US11039635B2 (en) | 2019-02-27 | 2021-06-22 | The Fynder Group, Inc. | Food materials comprising filamentous fungal particles |
US11272726B2 (en) | 2019-02-27 | 2022-03-15 | The Fynder Group, Inc. | Food materials comprising filamentous fungal particles and membrane bioreactor design |
US11478007B2 (en) | 2019-02-27 | 2022-10-25 | The Fynder Group, Inc. | Food materials comprising filamentous fungal particles and membrane bioreactor design |
US11432575B2 (en) | 2019-02-27 | 2022-09-06 | The Fynder Group, Inc. | Food materials comprising filamentous fungal particles and membrane bioreactor design |
US11118305B2 (en) | 2019-06-18 | 2021-09-14 | The Fynder Group, Inc. | Fungal textile materials and leather analogs |
US11447913B2 (en) | 2019-06-18 | 2022-09-20 | The Fynder Group, Inc. | Fungal textile materials and leather analogs |
US11427957B2 (en) | 2019-06-18 | 2022-08-30 | The Fynder Group, Inc. | Fungal textile materials and leather analogs |
US11414815B2 (en) | 2019-06-18 | 2022-08-16 | The Fynder Group, Inc. | Fungal textile materials and leather analogs |
US11649586B2 (en) | 2019-06-18 | 2023-05-16 | The Fynder Group, Inc. | Fungal textile materials and leather analogs |
US11718954B2 (en) | 2019-06-18 | 2023-08-08 | The Fynder Group, Inc. | Fungal textile materials and leather analogs |
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