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Статті в журналах з теми "Submerged culturing"
Dergham, Yasmine, Pilar Sanchez-Vizuete, Dominique Le Coq, Julien Deschamps, Arnaud Bridier, Kassem Hamze, and Romain Briandet. "Comparison of the Genetic Features Involved in Bacillus subtilis Biofilm Formation Using Multi-Culturing Approaches." Microorganisms 9, no. 3 (March 18, 2021): 633. http://dx.doi.org/10.3390/microorganisms9030633.
Повний текст джерелаSavin, P. S. "Technology of growing infectious material of Claviceps purpurea under submerged culturing conditions." Russian Agricultural Sciences 33, no. 2 (April 2007): 94–96. http://dx.doi.org/10.3103/s1068367407020085.
Повний текст джерелаBebök, Zsuzsanna, Albert Tousson, Lisa M. Schwiebert, and Charles J. Venglarik. "Improved oxygenation promotes CFTR maturation and trafficking in MDCK monolayers." American Journal of Physiology-Cell Physiology 280, no. 1 (January 1, 2001): C135—C145. http://dx.doi.org/10.1152/ajpcell.2001.280.1.c135.
Повний текст джерелаLai, Long-Shan T., Tai-Her Tsai, Te Chi Wang, and Tsung-Yao Cheng. "The influence of culturing environments on lovastatin production by Aspergillus terreus in submerged cultures." Enzyme and Microbial Technology 36, no. 5-6 (April 2005): 737–48. http://dx.doi.org/10.1016/j.enzmictec.2004.12.021.
Повний текст джерелаGuo-zhang, ZU, GUAN Yuan-liang, HOU Guan-jun LI Hai-yang, CHEN Yu, TUO Ji-liang, and ZHOU Guo-zhi. "Utilization and Protection of the Submerged Plant Resources by Pen-crab Culturing in Nushan Lake." Journal of Lake Sciences 11, no. 1 (1999): 91–96. http://dx.doi.org/10.18307/1999.0115.
Повний текст джерелаDomingos, Marcelo, Priscila Brasil de Souza-Cruz, André Ferraz, and Arnaldo Márcio Ramalho Prata. "A new bioreactor design for culturing basidiomycetes: Mycelial biomass production in submerged cultures of Ceriporiopsis subvermispora." Chemical Engineering Science 170 (October 2017): 670–76. http://dx.doi.org/10.1016/j.ces.2017.04.004.
Повний текст джерелаProtsenko, M. A., N. E. Kostina, and T. V. Teplyakova. "Selection of Nutrient Media for Submerged Culturing of Wood-Destroying Mushroom of Daedaleopsis tricolor (Bull.) Bondartsev et Singer." Biotekhnologiya 34, no. 1 (2018): 45–51. http://dx.doi.org/10.21519/0234-2758-2018-34-1-45-51.
Повний текст джерелаGHAZANFAR, MISBAH, MUHAMMAD IRFAN, HAFIZ ABDULLAH SHAKIR, MUHAMMAD KHAN, MUHAMMAD NADEEM, and AHMAD IRFAN. ""CELLULASE PRODUCTION OPTIMIZATION BY BACILLUS AERIUS THROUGH RESPONSE SURFACE METHODOLOGY IN SUBMERGED FERMENTATION "." Cellulose Chemistry and Technology 56, no. 3-4 (May 5, 2022): 321–30. http://dx.doi.org/10.35812/cellulosechemtechnol.2022.56.28.
Повний текст джерелаPetre, Alexandru, Mihaela Ene, and Emanuel Vamanu. "Submerged Cultivation of Inonotus obliquus Mycelium Using Statistical Design of Experiments and Mathematical Modeling to Increase Biomass Yield." Applied Sciences 11, no. 9 (April 30, 2021): 4104. http://dx.doi.org/10.3390/app11094104.
Повний текст джерелаNguyen Thi, Minh Huyen, Hoa Tran Thi, Tuyet Lan Ninh Thi, Le Pham Thi, Men Do Thi, and Hien Tran Thi. "Evaluation of microbiological and heavy metal safety assessment of Phellinus linteus mass powder from submerged fermentation." Heavy metals and arsenic concentrations in water, agricultural soil, and rice in Ngan Son district, Bac Kan province, Vietnam 3, no. 1 (March 22, 2020): 20–28. http://dx.doi.org/10.47866/2615-9252/vjfc.99.
Повний текст джерелаДисертації з теми "Submerged culturing"
Tanski, Erin M. "Culturing Vallisneria americana for Restoration Efforts." Thesis, University of North Texas, 2004. https://digital.library.unt.edu/ark:/67531/metadc4448/.
Повний текст джерелаПоліщук, Валентина Юріївна. "Розробка технології виробництва рибофлавіну і ефірної олії, що продукуються Eremothecium ashbyi Guill". Doctoral thesis, Київ, 2018. https://ela.kpi.ua/handle/123456789/23301.
Повний текст джерелаA well-known microorganism-producer of riboflavin is ascomycete Eremothecium ashbyi used in industry. Besides overexpression of riboflavin, E. ashbyi also performs synthesis of flavinadeninedinucleotide (FAD). Using E. ashbyi, one can obtain either forage riboflavin used as a feed additive for livestock, or, using certain isolation and purification methods, riboflavin of medical purpose. Concomitantly with riboflavin synthesis, E. ashbyi performs synthesis of essential oil, identical by its aroma and properties to essential oil derived from rose petals. It contains such aromatic substances as geraniol (69.5–84.5%), nerol, linalool, and β-phenylethanol (12.7–27.7%). This allows viewing E. ashbyi as a promising producer of aromatic substances, which are necessary for perfume and toiletry industry. Biotechnology of rose essential oil, one of the most valuable in the world, has not been developed so far. At present, manufacture of riboflavin using biotechnology is not established in Ukraine, and the potential of concomitant production of essential oil as well makes the topic of this thesis urgent, timely, and important. During the work, morphological and cultural peculiarities of the strain Eremothecium ashbyi F-340 have been investigated. It belongs to ascomycetes not generating ascocarps, has true dichotomic branched bright-yellow mycelium composed of multinucleate cells. Mycelium color is due to the presence of riboflavin, which is accumulated in such quantities that it is precipitated in vacuoles as crystals. Natural variability of the strain has been shown. The fungus forms pigmented yellow and orange colonies with high ability to riboflavin biosynthesis, and white colonies with low biosynthetic ability. Most frequently, white colonies develop upon archive culture reactivation and almost do not appear upon regular reinoculations and alterations of liquid and agar nutrient media. The strain storage conditions have been investigated. It has been established that short-term storage of E. ashbyi F-340 in the active state is possible on agar glucose-peptone-yeast and soybean media at storage temperature 5°C. Long-term storage of E. ashbyi culture (for 7 months) is possible only at room temperature. Temperature effects on viability of Eremothecium ashbyi F-340 mycelium have been investigated. The lower limit temperature for E. ashbyi is 4°С. The upper limit temperature is equal to 38°С. Minor growth of the fungus is still observed at this temperature, and at 39°С no mycelium growth is observed, and growth restoration at 28°С is not observed. Growth dynamics of E. ashbyi strain F-340 in submerged culture follows the known regularities for periodic cultures. Exponential growth phase lasts for about 2 days; after this, growth deceleration and culture switch into stationery growth phase are observed; the latter one lasts for about 5 days of culturing, after which the culture is switched into die-off or autolysis phase. It has been established that pH decrease to 5.2 occurs during intensive strain growth; intensive riboflavin accumulation in cultural fluid and biomass is associated with pH increase to 7.8. The most intensive riboflavin accumulation occurs in stationery growth phase on culturing day 3–4, and its concentration reaches 341,6 mg/dm3. The second stage of riboflavin accumulation occurs on day 5-7 and is associated with culture autolysis; riboflavin content reaches 55,22,7 mg/dm3. Riboflavin is accumulated at the beginning in E.ashbyi mycelium, where it reaches the level of 8.1-10.7 mg/g of dry biomass and remains at that level until completion of culturing. Despite continuous maintenance selection during the strain culturing under laboratory conditions for 3 years, gradual considerable decrease in riboflavin accumulation and relevant increase in biomass accumulation level has been observed. It is known from literature data that riboflavin overexpression by fungus E. ashbyi in natural conditions occurs as a defense reaction on the effect of sun ultraviolet radiation. That is why we suggested to perform UV irradiation of the producer in order to increase riboflavin synthesis. Irradiation of the producer cultural fluid results in increase of riboflavin biosynthesis by 72-74%, and irradiation of aqueous suspension of mycelium of the producer strain results in synthesis increase by 80%. It has been established that the highest riboflavin yield is achieved when the inoculum aged 3-4 days in quantity 1% is used. The effect of culturing conditions on biosynthetic ability of the producer has been investigated at the following stage. It has been shown that the initial pH level of media intended for biomass and riboflavin production has to be different. In order to obtain maximum quantities of biomass and inoculum, it is expedient to adjust the medium pH to the level 5.5–6.0, and for maximum riboflavin accumulation, initial medium рН has to be 7.5. It has been established that, under aeration conditions on a rocker at 180 rpm, 70 % more riboflavin is synthesized compared to 70 rpm. E. ashbyi is capable to growth in a wide range of temperatures from 20 to 38С. The optimal temperature for maximum target product yield is 27-29С. The effect of various carbon sources on biomass accumulation and riboflavin synthesis by E. ashbyi strain F-340 has been studied. Monosaccharides (fructose, galactose) and hexatomic alcohol sorbitol are better suitable for riboflavin synthesis, and biomass is accumulated better in the presence of fructose, sucrose, and glycerol in the medium. The best nitrogen source for E.ashbyi F-340 turned out to be yeast extract; riboflavin quantity synthesized in a medium with yeast extract was 54% more compared to other nitrogen sources. Nevertheless, no medium for Eremothecium ashbyi culturing containing the said carbohydrates and being cheap and technological enough has been suggested yet. In order to solve this problem, we have suggested to use such a promising natural carbon source as glucose-fructose syrup (GFS), manufactured from corn starch via its enzymatic hydrolysis to glucose with following isomerization of glucose parts into fructose and further purification. It has been shown that the highest vitamin quantity is synthesized with the use of GFS-10 (140 mg/dm3), which is 7 times as high as in a medium with glucose, and 3.8 times as high as in a medium with fructose. For the nutrient medium optimization, we have planned a complete factorial experiment at two levels for 3 factors; the planning matrix was supplemented with “star” points, and orthographic central composite design of second order for 3-factor experiment has been obtained. As a result of calculations, regression equation of the second order has been obtained. Statistical significance of the equation coefficients was verified according to Student’s criterion, and adequacy of the obtained equation was verified according to Fisher’s criterion. As a result of mathematical processing of experimental data, we have obtained the regression equation of relation between riboflavin concentration in cultural fluid and concentrations of GFS-10 (m), yeast extract (w) and peptone (v): Y1= –758.483+41.029·m+9.959·w+5.777·v+0.693·m·w–0.472·m·v–3.51·w·v– –0.547·m2+5.701·v2 Analyzing the response surfaces, we have established the composition of modified medium: optimal GFS-10 concentration for maximum riboflavin accumulation is 40 g/dm3, and concentrations of yeast extract and peptone in the medium are 10 and 1 g/dm3, respectively. Riboflavin concentration observed during culturing on modified medium in cultural fluid is 350.4 mg/dm3, which is 17 times higher than on GPY medium and 2.5 times higher than on initial medium with GFS- 10. Testing of essential oil content in cultural medium was performed via triple extraction with hexane with further removal of the solvent. Wide range of variation of essential oil content has been shown. The highest quantity is observed in the medium containing GFS-10 (273…420 mg/dm3) as carbon source. Essential oil quantity is increased with increase of GSF concentration in the medium. Technological flow chart for concomitant production of riboflavin and essential oil production by hydrodistillation with further separation of riboflavin and essential oil isolation flows is provided. Scientific novelty of the obtained results: - growth dynamics, biomass yield, riboflavin and essential oil accumulation by the selected producer strain Eremothecium ashbyi have been investigated in media with different nutrition sources; - composition and acid content of media, favorable for the growth of the producer strain in submerged culture, have been determined; - rational biotechnological parameters for achievement of maximum riboflavin and essential oil yield have been determined: culturing temperature 27-29С, initial medium pH 7,5, stirring 180 rpm; - nutrient medium for riboflavin and essential oil accumulation has been optimized using experiment planning methods (such medium includes GFS-10, yeast extract and peptone), and possibility of concomitant production of these products has been verified; - biotechnology for riboflavin and essential oil production from domestic renewable raw material – glucose-fructose syrup manufactured from corn – has been scientifically justified are developed for the first time.
張文菀. "Effect of different submerged culturing conditions on mycelium growthand polysaccharide formation from Antrodia camphorata." Thesis, 2003. http://ndltd.ncl.edu.tw/handle/35569367427683233964.
Повний текст джерела東海大學
食品科學系
91
Antrodia camphorata is a valuable herb, and only grown in Taiwan. It can strengthen the immune system of human body. At the present time, the cultivation of fructification of A. camphorata has not been successful. The purpose of this study is by using submerged cultures of A. camphorata, to exam culture conditions for the mycelium growth and its polysaccharide formation. The results show that, the uptimaml condition in shake flask cultivations of A. camphorat mycelium and polysaccharide formation is at 28℃, with initial pH 5, at rotating speed 100 rpm and inoculum size 5% (v/v). The 500 ml Erlenmeyer flask without baffle and containing 100 ml medium, after 14 days cultivation, the maximal mycelium dry weigh is 448 mg per 100 ml, exopolysaccharide is 0.837 mg per ml. Culture conditions were adapted to cultivate A. camphorat by different fermentors, at 28℃, agitation speed 100 rpm, and aeration rate 0.5 vvm. After 14 days fermentation, the mycelium dry weight for 7 L Airlift fermentor (AL) was 7.09 g/L; for 5 L stirred tank fetmentor with Marine impeller (MST) was 5.99 g/L; and for 5 L stirred tank fetmentor with turbine disk impeller (TDS) was 5.68 g/L, in compare with 5.48 g/L of the shake flasks. After 14 day fermentation, the microbial polysaccharide formation in the TDS fermentor was low, as compared to the other two fermentors. The concentration of exopolysaccharide and endopolysaccharide in TDS was 0.763 mg/ml and 0.144 mg/ml respectively, while in MST fermentor was 0.873 mg/ml and 0.246 mg/ml; and in AL fermentor, which was the highest, was 1.016 mg/ml and 0.398 mg/ml respectively. The improvement on the TDS fermentor in mycelium growth and polysaccharide production by using MST and AL fermentor would be beneficial in reducing the production cost of the submerged cultures of A. camphorata mycelium.
Chen, Hung-Hui, and 陳宏慧. "Effect of submerged culturing condition on mycelium growth and formation of polysaccharides from Wolfiporia cocos." Thesis, 2005. http://ndltd.ncl.edu.tw/handle/99039886672569344754.
Повний текст джерела東海大學
食品科學系
93
Abstract Wolfiporia cocos is an edibles fungi, it has long been used as traditional Chinese herb with curing incontinence, edema, sputum, palpitations and sleeplessness. Pharmacology studies have proven that its anti-tumor, anti-emetic, ant-inflammation, anti- nephritis, diabetes. The potential markets for W.cocos as neutraceutial and pharmaceutical products will stimulate the research for methods of its cultivation. The results indicated that in shake flask fermentation at 26ºC, 100rpm, a 5% olive oil addition in the medium is the best among different concentrations for the mycelium growth, while the 4% olive favors the exo-polysaccharide formation. In fermentor studies, the 7 liter bubble column fermentor (BCF) with 2 vvm aeration is the best for exo-polysaccharide production, and has a concentration of 0.39mg/ml in 7 days,as compared to 0.23mg/ml by 5 liter stirred tank fermentor(STF) at 2 vvm . At 1 vvm, the polysaccharide is 0.17 mg/ml and 0.21 mg/ml for BCF and STF, respectively.Lower aeration rate resulted in poor polysaccharide production which is caused by the aggregation of the mycelium which accumulated at the bottom of fermentor, and interfered the air supply. The fermentation condition affect the molecular weight (MW) of the polysaccharides greatly. MW distribution of polysaccharides, as determined by GPC, from STF 1vvm, BCF 2vvm, and BCF 0.5vvm, were in the rang of 103~108Da, and during the 7 days fermentation, the MW changed from one single distribution in early stage into two MW distribution in the late stage. STF 2vvm and BCF 0.5 vvm was in the range of 103~109Da, while the MW was unchanged throught the cultivation period.
Liu, Tzu-hsin, and 劉慈欣. "Effect of submerged culturing conditions on mycelium growth and formation of useful components from Cordyceps militaris." Thesis, 2004. http://ndltd.ncl.edu.tw/handle/20186728940165841094.
Повний текст джерела東海大學
食品科學系
92
Abstract North-Cordyceps, also known as “Pupa-Cordyceps” is a popular and precious Chinese folk medicine. It growes from pupa with fruiting body by fungus Cordyceps militaris in nature. Due to the environmental impact, production of natural Cordyceps militaris is limited. Fermentation of C.militaris using submerged cultures to produce the mycelium and its useful components as the supply of market need is already on the way by the food and pharmaceutical industries. We found that in shake flask study, a 2% sunflower oil addition in the medium improved the mycelium growth and formation of useful components. Batch fermentation in the 7L airlift fermentor with 2vvm aeration rate resulted in 37.0mg/ml mycelium dry weight, 415μg/ml adenosine, 665μg/ml cordycepin and 2.31mg/ml polysaccharide, which is the hest as compared to 1vvm or 0.5vvm in the 11days fermentation. The airlift fermentor, in general, is better than stirred tank fermentor in regard to C.militaris cultivation. When C.militaris fermentation run by the fed-batch method, where the half of sugar substrate were added at the 3rd day of the fermentation higher cell concentration, polysaccharide, adenosine and cordycepin were found both in airlift and stirred tank fermentors as compared to batch process. However, controlling pH at 4.5 or 6.0 in the fermentor showed poor effect on mycelium growth and the formation of adenosine, cordycepin and polysaccharide as compared to uncontrolled pH where the initial fermentation started at pH 6.0. Key word : C.militaris, adenosine, cordycepin, stirred tank fermentor, airlift fermentor, fed-batch culture
Hsiao, Meiling, and 蕭美玲. "Effect of submerged-culturing conditions and different types of fermentors on exopolysaccharide production by Agaricus blazei Murrill." Thesis, 2007. http://ndltd.ncl.edu.tw/handle/00234177038731613938.
Повний текст джерела東海大學
食品科學系
95
Abstract Agaricus blazei Murrill, an edible and medicinal mushroom originally grown in Brazil, was recently developed as a functional food. The metabolites of this mushroom from submerged culture were proved to have unique biological activity such as antitumor, antioxidative and immunity-stimulating capabilities. This research was aimed to study the effects of submerged-culturing conditions and different types of fermentors on the production and functional properties (molecular weight, antibacterial and antioxidative activities) of exopolysaccharide (EPS) by A. blazei. Results showed that the optimal submerged-culturing conditions were : incubation temperature of 25℃, initial pH of 5.4, culture volumes of 50ml, corn steep liquor at 0.3% (w/v), fructose at 4% (w/v), yeast extract at 0.4% (w/v), and a C/N ratio (fructose / yeast extract) of 10. The maximal yields of EPS and mycelial biomass, 0.302 and 25.2 g/l, respectively, were reached on the 14th day of incubation from shake flask culture under the optimized culturing conditions. A shorter incubation time for maximal EPS and mycelial production (7~10 vs. 14 days), greater EPS yield (3.20~6.96 vs. 0.302 g/l) and higher mycelial biomass (42.01~46.70 vs. 25.22 g/l) were obtained from cultures of fermentors as compared with those from shake flask culture. Among the three types of fermentors, the agitated fermentor showed the highest specific growth rate (μ=0.476 day-1) and the lowest EPS formation rate (Qp=0.46 g/l/day). On the contrary, the air lift fermentor demonstrated the lowest specific growth rate (μ=0.365 day-1) and the highest EPS formation rate (Qp=0.77 g/l/day). As for specific EPS yield (Yp/x), EPS yield (Yp/s) and biomass yield (Yx/s), results showed an increasing tendency of air lift fermentor > air bubble fermentor > agitated fermentor. Cultures of fermentors had higher and broader spectrum of antibacterial activies than shake flask culture. The inhibitory capability also demonstrated the same order as : air lift fermentor > air bubble fermentor > agitated fermentor. The bacterial strains susceptible to fermented cultures were : Bacillus cereus, Salmonella typhimurium, Staphylococcus aureus, Enterococcus faecalis, Enterobacter aerogenes, Escherichia coli, Proteus vulgaris, Listeria monocytogenes, Shigella dysenteriae and Pseudomonas aeruginosa. Among the ten strains, B. cereus was the most susceptible one. This finding could be applied to use the culture broth of A. blazei as a potential biopreservative. Same major molecular weights (2.5×105 and 3.0×103 Da) and molecular weight distribution (7.4×104~2.1×106 Da) were observed for EPS from the three batch cultures of fermentors. The EPS from culture of air lift fermentor had higher content of molecular weight of 2.5×105 Da. The antioxidative activity (DPPH scavenging effect) of the three fermented cultures was equal or higher than that of control antioxidants. Under the same concentration, the fermented culture of air lift fermentor presented the highest antioxidative activity. As far as the EPS yield, the mycelial biomass production, the formation rates of EPS and mycelial biomass, and the antibacterial and antioxidative activities of fermented cultures were concerned, all above results showed a trend of air lift fermentor > air bubble fermentor > agitated fermentor. In conclusion, using the air lift fermentor, which has lower shearing force and better convective circulation as compared with agitated and air bubble fermentors, could produce higher yield of EPS from A. blazei with better functional properties.
Lo, Kuo Yen, and 羅國晏. "Effect of submerged culturing conditions and types of fermentors on production and bioactivity of exopolysacchirades by Phellinus igniarius." Thesis, 2008. http://ndltd.ncl.edu.tw/handle/08419809035568651446.
Повний текст джерела東海大學
食品科學系
97
The exopolysaccharides (EPS) from many mushrooms have been reported to possess important biological functions including anti-tumor, immuno-stimulating, hypoglycemic and antioxidative capacities. Phellinus igniarius PI, a potently medicinal and EPS-producing mushroom, was selected in this research to study the effect of submerged culturing condition and different types of fermentors on the production and the bioactivity (molecular weight, relative β-(1→3)-D-glucan content, antimicrobial and antioxidative activities) of EPS by P. igniarius PI. Results showed that factors for optimal submerged-culturing condition were : incubation temperature of 30℃, glucose at 1% (w/v), yeast extract at 1% (w/v), corn steep liquor at 0.3% (w/v), initial pH of 5.4, and a C/N ratio (glucose / yeast extract) of 1.0. Under this optimized culturing condition, maximal yields of mycelial biomass (9.39 g/l) and EPS (1.93 g/l) were reached on the 8th day of incubation from shake flask culture and increased 2.4 and 10.1 times, respectively, as compared with those of the basal medium. Among the three types of fermentors, the stirred-tank fermentor showed the highest specific growth rate (μ=0.88 day-1). The air bubble fermentor showed the highest biomass yield (Yx/s=122.29 mg/g) and EPS formation rate (QP=0.39 g/l/day). As for specific EPS yield (Yp/x) and EPS yield (Yp/s), results showed an increasing tendency of air bubble fermentor > stirred-tank fermentor > air lift fermentor. The EPS of P. igniarius PI demonstrated no antibacterial activies against the six bacterial strains (Bacillus cereus BCRC 10250, Escherichia coli BCRC 10239, Micrococcus luteus BCRC 10449, Pseudomonas aeruginosa BCRC 10261, Staphylococcus aureus BCRC 10451 and Salmonella typhimurium BCRC 10241) tested. Same molecular weight (4000 Da) was found in EPS from the shake flask and three different types of fermentors. The EPS from culture of air bubble fermentor had higher content of molecular weight of 4000 Da. Under same concentration (10g/l), the fermented cultures from stirred-tank and air bubble fermentors showed the highest DPPH scavenging effect (86.94%, IC50=4.83g/l) and total antioxidant capacity (93.26%, IC50=1.52g/l), respectively, among those from shake flask and three different types of fermentors.The EPS from air bubble fermentor also had the highest relative β-(1→3)-D-glucan contents. As mentioned above, using air bubble fermentor, which has lower shearing force and better mixing effect as compared with stirred-tank and air bubble fermentors, could produce higher yield of EPS from Phellinus igniarius PI with better bioactivity. Replacing reagent-grade medium components with food-grade components not only reduced the production cost of EPS but also increased the yields of mycelial biomass (5.76 g/l) and exopolysaccharide (3.74 g/l) 2.4 and 10.1 times, respectively. In addition, the food-grade medium components offered a better buffering effect.