• 반도체디스플레이기술학회지
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• 제19권4호
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• pp.65-70
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• 2020

CNN's technologies that represent emotional detection include primitive CNN algorithms, deployment normalization, and drop-off. We present the methods and data of the three experiments in this paper. The training database and the test database are set up differently. The first experiment is to extract emotions using Batch Normalization, which complemented the shortcomings of distribution. The second experiment is to extract emotions using Dropout, which is used for rapid computation. The third experiment uses CNN using convolution and maxpooling. All three results show a low detection rate, To supplement these problems, We will develop a deep learning algorithm using feature extraction method specialized in image processing field.

• Journal of Microbiology and Biotechnology
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• 제22권6호
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• pp.826-831
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• 2012

Acarbose, a pseudo-oligosaccharide, is widely used clinically in therapies for non-insulin-dependent diabetes. In the present study, S-adenosylmethionine (SAM) was added to selected media in order to investigate its effect on acarbose fermentation by Actinoplanes utahensis ZJB-08196. Acarbose titer was seen to increase markedly when concentrations of SAM were added over a period of time. The effects of glucose and maltose on the production of acarbose were investigated in both batch and fed-batch fermentation. Optimal acarbose production was observed at relatively low glucose levels and high maltose levels. Based on these results, a further fed-batch experiment was designed so as to enhance the production of acarbose. Fed-batch fermentation was carried out at an initial glucose level of 10 g/l and an initial maltose level of 60 g/l. Then, 12 h post inoculation, 100 ${\mu}mol/l$ SAM was added. In addition, 8 g/l of glucose was added every 24 h, and 20 g/l of maltose was added at 96 h. By way of this novel feeding strategy, the maximum titer of acarbose achieved was 6,113 mg/l at 192 h. To our knowledge, the production level of acarbose achieved in this study is the highest ever reported.

• 상하수도학회지
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• 제8권3호
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• pp.1-8
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• 1994

In the general process of design for aerobic digestion, the design for field plant of which inflow pattern is continuous inflow is performed using the results from lab scale batch reactor. However, the recent researchers reported that the general designs were performed as over-estimated, Therefore, in this study, laboratory batch experiments were carried out at $20^{\circ}C$ and pH 7.5 on the aerobic digestion of waste activated sludge at different solid levels. This treatise could consider the negligence about effective digestion periods the usage of VSS as solid concentration, and the effect of initial solid concentration of solid degration rate coefficient($k_d$) as reasons of the overestimated design, and showed the scheme of how to design for aerobic digestion from batch experiment.

• Biotechnology and Bioprocess Engineering:BBE
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• 제8권5호
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• pp.291-293
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• 2003

Batch reactors were employed to investigate the kinetics of cellulose hydrolysis under extremely low acid (ELA) and high temperature condition. The sawdust was pretreated by Auto-hydrolysis prior to the batch reaction. The maximum yield of glucose obtained from the batch reactor experiment was about 70% for the pretreated sawdust, this occurred at 210 and 22$0^{\circ}C$. The maximum glucose yield from the untreated sawdust was much lower at these temperatures, about 55%. The maximum yields of glucose from the lignocellulosics were obtained between 15th and 20th minutes after which gradual decrease was observed.

• 생명과학회지
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• 제17권11호
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• pp.1582-1586
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• 2007

균주 JH232가 생성한 bacterial cellulose (BC)는 이온교환 막 생산을 위한 환경친화적 재료로서 잠재능이 있다는 것이 전 연구(J. of Chem. Technol. Biotechnol. 2004, 79, 79-84)를 통해 보고되었다. 본 연구를 통해 JH232를 동정하였으며 BC 생성 특성을 조사하였다. 16S rRNA 유전자의 비교분석을 통해 JH232는 Gluconacetobacter sp.인 것을 밝혀냈다. 플라스크실험 결과 이 균주는 초기 pH 5.5로 조절된 CSL 배지에서 온도가 $30^{\circ}C$인 조건하에 배양하였을 때 BC 생성량이 최대를 나타내었다. 발효조 실험을 통해서 회분식 배양보다 유가배양에 의해 JH232의 BC 생성량이 1.56배 더 높게 나타났다.

• Journal of Microbiology and Biotechnology
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• 제19권9호
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• pp.972-981
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• 2009

In this paper, a fed-batch cultivation process in recombinant Escherichia coli BL21(DE3) bacteria, for the production of human soluble catechol-O-methyltransferase (hSCOMT), is presented. For the first time, a straightforward model is applied in a recombinant hSCOMT expression system and distinguishes an initial cell growth phase from a protein production phase upon induction. Specifically, the kinetic model predicts biomass, substrate, and product concentrations in the culture over time and was identified from a series of fed-batch experiments designed by testing several feed profiles. The main advantage of this model is that its parameters can be identified more reliably from distinct fed-batch strategies, such as glycerol pulses and exponential followed by constant substrate additions. Interestingly, with the limited amount of data available, the proposed model accomplishes satisfactorily the experimental results obtained for the three state variables, and no exhaustive process knowledge is required. The comparison of the measurement data obtained in a validation experiment with the model predictions showed the great extrapolation capability of the model presented, which could provide new complementary information for the COMT production system.

• 한국지하수토양환경학회지:지하수토양환경
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• 제17권6호
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• pp.92-101
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• 2012

Korea shows the soil pH is 5.8 ~ 6.2 by many factors including the geological structure and climate condition. There is known as the cause for soil acidification by weathering of the mineral, excessive use of the chemical fertilizer, and extensively diffused acid rain. The purpose of research is environmentally-friendly material neutralization technology development utilizing the waste resources against by acid soil. The experiment analyze the physico-chemical property of the acid soil and waste resource materials (waste lime, oyster shell, bottom ash). The Batch-Test was performed under 3 stage. As a result, the acid soil showed up acid soil about 3.19. And waste lime, oyster, bottom ash showed the alkalinity with 9.62, 10.08, 9.17. In case of 1 batch-test experimental result, waste lime and oyster shell, the alkalinity was shown over 7.5 and the good efficiency was showed, on the other hands, the bottom ash showed the pH 4 the neutralization efficiency which is low. waste resource materials to be applied to 2 steps was chosen as the waste lime except the bottom ash and oyster. In 2 step batch-test experiment, it was exposed to be the most appropriate in case of doing the combination ratio of the waste lime and oyster shell with 9 : 1. It was exposed to be efficient most in the effeciency and aspect of economical efficiency combination ratio of the soil and materials was 9.6 : 0.6 with 3 step batch-test experimental result.

• 한국지반환경공학회 논문집
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• 제15권8호
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• pp.45-50
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• 2014

하수관 내에서의 하수와 미생물의 반응에 대한 실험은 이미 매설된 하수관에 적용할 경우 실험조건의 변화가 제한적이며 실험시간에도 한계가 있다. 본 연구에서는 이러한 하수관 내에서의 하수와 미생물의 반응에 대하여 DO를 제한 조건으로 설정하였을 경우, 실험실 내에서 실험반응조를 통해 재현하는 방법에 대하여 연구하였다. 하수관 내에서의 DO 농도는 기상 중의 산소가 하수 내로 이동하는 재포기현상에 의해 조절된다. 이러한 현상을 이용하여 임의로 실험반응조에서 하수관 내의 유하조건을 조절하고 재포기현상을 재현하여 유하조건과 재포기계수와의 상관관계를 얻을 수 있으며, 교반강도(속도경사)에 따른 재포기계수와 하수관거에서의 유하조건에 따른 재포기계수의 상관관계를 통해 동일한 재포기계수 값을 갖는 교반강도와 유하조건을 설정할 수 있다. 이러한 결과를 통해 재포기계수를 제한인자로 설정하여 실험을 실시할 경우 하수관거에서의 상황을 실험반응조를 통해 재현할 수가 있었다.

• 한국항공우주학회지
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• 제46권2호
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• pp.133-140
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• 2018

본 논문에서는 복합재 적층 구조물의 면내 구조 해석을 위한 자동화 소프트웨어를 개발한다. 개발된 소프트웨어는 다양한 파손 기준을 제공하며 사용자의 편리성을 고려하여 해석 결과를 출력한다. 또한 병렬처리 기법에 기반한 일괄 처리 해석(batch job analysis) 기능을 지원한다. 구현된 소프트웨어의 성능을 검증하기 위하여 소프트웨어에서 계산된 안전 여유와 자체적으로 사용 중인 in-house 방식과 실제 시편 실험에서 얻어진 안전 여유간의 비교를 수행하였다. 비교 결과 in-house 방식과는 0.01 이하의 오차가 있었으며 시편 실험과는 약 ${\pm}10%$ 이내의 오차가 존재함을 확인하였다. 또한 병렬처리 기법을 적용한 일괄 처리 해석 작업의 실행 속도 개선을 확인하였다.

• Environmental Engineering Research
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• 제19권2호
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• pp.157-163
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• 2014

The adsorption of Cr(VI) from aqueous solutions to activated carbon fiber (ACF) was investigated using both batch and flow-through column experiments. The batch experiments (adsorbent dose, 10 g/L; initial Cr(VI) concentration, 5-500 mg/L) showed that the maximum adsorption capacity of Cr(VI) to ACF was determined to 20.54 mg/g. The adsorption of Cr(VI) to ACF was sensitive to solution pH, decreasing from 9.09 to 0.66 mg/g with increasing pH from 2.6 to 9.9; the adsorption capacity was the highest at the highly acidic solution pHs. Kinetic model analysis showed that the Elovich model was the most suitable for describing the kinetic data among three (pseudo-first-order, pseudo-second-order, and Elovich) models. From the nonlinear regression analysis, the Elovich model parameter values were determined to be ${\alpha}$ = 162.65 mg/g/h and ${\beta}$ = 2.10 g/mg. Equilibrium isotherm model analysis demonstrated that among three (Langmuir, Freundlich, Redlich-Peterson) models, both Freundlich and Redlich-Peterson models were suitable for describing the equilibrium data. In the model analysis, the Redlich-Peterson model fit was superimposed on the Freundlich fit. The Freundlich model parameter values were determined to be $K_F$ = 0.52 L/g and 1/n = 0.56. The flow-through column experiments showed that the adsorption capacities of ACF in the given experimental conditions (column length, 10 cm; inner diameter, 1.5 cm; flow rate, 0.5 and 1.0 mL/min; influent Cr(VI) concentration, 10 mg/L) were in the range of 2.35-4.20 mg/g. This study demonstrated that activated carbon fiber was effective for the removal of Cr(VI) from aqueous solutions.