• Journal of Microbiology and Biotechnology
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• v.16 no.11
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• pp.1690-1698
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• 2006

In order to investigate the effect of dissolved oxygen (DO) level on AVM $B_{1a}$ production by a high yielding mutant of Streptomyces avermitilis, five sets of bioreactor cultures were performed under variously controlled DO levels. Using an online computer control system, the agitation speed and aeration rate were automatically controlled in an adaptive manner, responding timely to the oxygen requirement of the producer microorganism. In the two cultures of DO limitation, the onset of AVM $B_{1a}$ biosynthesis was observed to casually coincide with the fermentation time when oxygen-limited conditions were overcome by the producing microorganism. In contrast, this phenomenon did not occur in the parallel fermentations with DO levels controlled at around 30% and 40% throughout the entire fermentation period, showing an almost growth-associated mode of AVM $B_{1a}$ production: AVM $B_{1a}$ biosynthesis under the environments of high DO levels started much earlier than the corresponding oxygen-limited cultures, leading to a significant enhancement of AVM $B_{1a}$ production during the exponential stage. Consequently, approximately 6-fold and 9-fold increases in the final AVM $B_{1a}$ production were obtained in 30% and 40% DO-controlled fermentations, respectively, especially when compared with the culture of severe DO limitation (the culture with 0% DO level during the exponential phase). The production yield ($Y_{p/x}$), volumetric production rate (Qp), and specific production rate (${\bar{q}}_p$) of the 40% DO-controlled culture were observed to be 14%, 15%, and 15% higher, respectively, than those of the parallel cultures that were performed under an excessive agitation speed (350 rpm) and aeration rate (1 vvm) to maintain sufficiently high DO levels throughout the entire fermentation period. These results suggest that high shear damage of the high-yielding strain due to an excessive agitation speed is the primary reason for the reduction of the AVM $B_{1a}$ biosynthetic capability of the producer. As for the cell growth, exponential growth patterns during the initial 3 days were observed in the fermentations of sufficient DO levels, whereas almost linear patterns of cell growth were observed in the other two cultures of DO limitation during the identical period, resulting in apparently lower amounts of DCW. These results led us to conclude that maintenance of optimum DO levels, but not too high to cause potential shear damage on the producer, was crucial not only for the cell growth, but also for the enhanced production of AVM $B_{1a}$ by the filamentous mycelial cells of Streptomyces avermitilis.

• Korean Journal of Fisheries and Aquatic Sciences
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• v.25 no.4
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• pp.301-306
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• 1992

In order to determine the optimal conditions for the process of acetic acid fermentation, the kinetics of Acetobacter aceti fermentation in submerged batch cultures were studied at different agitation speeds and air flow rates. The maximum cell concentration was noted after about 48 hr fermentation and the time course of Acetobactey aceti fermentation showed a distinct feature of growth-associated product formation. At agitation speeds 700, 500, and 300 rpm fixed on air flow rate 1 v/v/M, specific grow rates were $3.97\times10^{-2},\;3.82\times10^{-2},\;and\;2.04\times10^{-2\} \;hr^{-1}$, saturation constants were 61.4, 64.6, and 69.4mg/ml. and volumetric oxygen transfer coefficients were 0.9337, 0.4468, and 0.1701 $min^{-1},$ respectively. At air flow rates 1.25, 1.00, and 0.75 v/v/M fixed on agitation speed 500 rpm, specific growth rates were $3.90\times10^{-2},\;3.82\times10^{-2},\;and\;2.37\times10^{-2}\;hr^{-1}$, saturation constants were 63.4, 64.6, and 64.9 mg/ml, and volumetric oxygen transfer coefficient were 0.4923, 0.4468, and 0.3509 $min^{-1},$ respectively.

• Journal of Life Science
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• v.20 no.10
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• pp.1433-1442
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• 2010

Parameters related to dissolved oxygen for the production of pullulan by Aureobasidium pullulans HP-2001 were optimized in 7 l and 100 l bioreactors. The optimal concentrations of glucose and yeast extract for the production of pullulan were 50.0 and 2.5 g/l, respectively, and its conversion rate from glucose was 37% at a flask scale. The optimal initial pH of the medium and temperature for cell growth were 7.5 and $30^{\circ}C$, whereas those for the production of pullulan were 6.0 and $25^{\circ}C$. The optimal agitation speed and aeration rate for cell growth were 600 rpm and 2.0 vvm in a 7 l bioreactor, whereas those for the production of pullulan were 500 rpm and 1.0 vvm. The production of pullulan with an optimized agitation speed of 500 rpm and aeration rate of 1.0 vvm was 18.13 g/l in a 7 l bioreactor. Maximal cell growth occurred without inner pressure, whereas the optimal inner pressure for the production of pullulan was 0.4 kgf/$cm^2$ in a 100 l bioreactor. The production of pullulan under optimized conditions in this study was 22.89 g/l in a 100 l bioreactor, which was 1.38 times higher than that without inner pressure.

• Applied Chemistry for Engineering
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• v.21 no.5
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• pp.488-494
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• 2010

Under W/O emulsion method using a homogenizer, ${\alpha}$-alumina powder was prepared to evaluate the effects of experimental conditions on its properties, such as particle shape, extent of aggregation, average particle size and distribution. The experimental parameters were the change of type, quantity and composition of emulsifiers as well as the change of O : W volumetric ratio and agitation rate. As results, in the case of the use of single surfactant of SP80, sphere-like particles could be prepared and the average particle size was hardly affected by the agitation speed more than 16000 rpm regardless of SP80 quantity used. When the extent of aggregation among sphere-like particles prepared using $HLB_m$ = 5 of [SP80 & TW80] was compared with that prepared using SP80 at the same vol% surfactant and agitation speed, the former showed more or less low aggregation phenomena and average particle size was slightly reduced. In addition, the fraction of nano-sized particles with low aggregation was increased by the use of 0.1 vol% n-butanol, as a co-surfactant, with $HLB_m$ = 5 of [SP80 & TW80].

• Journal of the Korean Society of Food Science and Nutrition
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• v.23 no.5
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• pp.845-848
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• 1994

The fermenting conditions for acetic acid production with Acetobacter sp. FM-10 which could grow in the medium containing 10% ehtanol were investigated. Initial concentration of acetic acid in broth medium affected greatly to the fermentation speed. For example , the acetic acid production increased proportionally by the increasing of initial concentration was higher that 1.0%. When the cultivation was started with broth medium containing 5% ethanol, the additional adding ethanol during the fermentation was not significantly increased the acidity of the medium. The acidity of the medium containing 10% ethanol was reached to 8.3% after shaking than static cultivation by about 10 days with 150 rpm shaking speed. Acetic acid production with shaking cultivation was faster the static cultivation by abot 10 days under the same condition except shaking. In acetic acid fermentation with the batch style fermentor , the optimum fermentation condition was 700 rpm of agitation speed and 5L/min air flow rate in 3L culture medium .

• Journal of the Korean institute of surface engineering
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• v.22 no.2
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• pp.78-87
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• 1989

Mechanism of formation of electroless composite coatings is similar to that of electrodeposited composite coating, but the amount of particles entraped in electroless coating is higher that the one of electrodeposited coatings. The methol of entrapment by the metal for SiC and Al2O3 particles is different from that for WC particles. In the former case the particles are gracually engulfed by the depositing metal, wheran with WC a metal envelope is rapidly fomed around each particles. This difference can be attributed to the difference in electrical resistivity of the particles. Inclusion density of SiC and Al2O3 particles during copeposition depend on the particle size, agitation condition, vabration conditions and electrolyte temperatures.

• The Korean Journal of Food And Nutrition
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• v.9 no.3
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• pp.236-241
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• 1996

Starter cultures were developed for the extension of the shelf life of bread. Lactobacillus plantarum and Bifidoacterium longum were selected as the mixed culture with Propionibacterium freudenreichii. P. fredenreichii with B. longum and L. plantarum produced 2.261% and 1.715% total acid, and pH value of cultured solutions was near 3.95. Propionic acid was produced 14 ~16 mg/ml by P. freudenreichii with L. plantarum and B. longum during 17 days, which was more than that of L. brevis. The pH values of the bread were 4.83 and 4.89 in respect to B. longum and L. plantarum when the fermented products were used to make the bread. Mold was not found for 10 days of storage of the bread at room temperature when the fermented products of B. longum were used for making bread. 37$^{\circ}C$, pH 6.0 and the lowest agitation were optimum conditions for the production of propionic acid in the scaled up fermentation.

• Microbiology and Biotechnology Letters
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• v.9 no.1
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• pp.1-6
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• 1981

Crystallization conditions of disodium guanosine-5'-monophosphate (5'-GMP. 2Na) were studied. The solubility of 5'-GMP. 2Na was decreased by addition of methanol and the optimum condition was as follows. The crystallization was carried out at 45$^{\circ}C$ with agitation rate of 160-200 rpm., which is Reynold's No. of 25, 000-32, 000. When concentration of methanol was 7.5%~10.0%, the 5'-GMP. 2Na was easily crystallized by addition of crystal seed.

• The Korean Journal of Food And Nutrition
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• v.12 no.2
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• pp.170-176
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• 1999

Optimum preparation conditions of Korean traditional sweet rice drink 'malt-Sikye' were 1hour of rice soaking time 30min of malt extraction time 60$^{\circ}C$ of malt extraction tem-perature 60$^{\circ}C$ of saccharification temperature 1hour of agitation interval 5hour of saccharification time 5.5 of pH 4% of malt concentration and 20% of rice content. The malt-Sikhy contained to 17.1% of total sugar 11.2% of reducing sugar o.34mg/ml of protein and 4.7${\mu}$mol/ml of amino acid. The most abundant sugar found in malt-Sikhye was maltose. The commercial amylolytic enzymes were not effec-tive in preparation malt-Sikye.

• Journal of the Korean Society for Precision Engineering
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• v.18 no.4
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• pp.135-141
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• 2001

An experimental study to find the effect of processing parameters for self-healing microcapules is performed. These microcapsules can be applied to accomplish the healing of delamination damage in woven E-glass/epoxy composites. This paper introduces the self-healing concept and presents a method for solving the microcapsule size and shape. Additionally, processing parameters are varied during the formation of microcapsules and these capsules are observed through optical microscope. To obtain thermogravimetric(TG) curve for the manufactured microcapsules, TGA tests are executed. From these results, the best processing conditions for the formation of capsules are found as follows: (1) temperature of solution $ 50^{\circ}C$, (2) potential of hytdrogen(pH) 3.5ppm, and (3) agitation 500~600rpm.