• Food Science and Preservation
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• v.21 no.1
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• pp.129-139
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• 2014

This study was conducted in order to investigate the optimal fermentation periods of the Smilax china L. leaves as a fermented tea via Aspergillus oryzae for 0 (non-fermented), and 10, 20, and 30 days (NF, F10, F20, F30). It was also observed for its quality characteristics. In the color and spectrum (400~700nm) of 1% tea water extract, NF was light yellow, whereas fermented tea (F10~F30) was light red color, and the F10 among F10~F30 has the clearest color and spectrum. Furthermore, acceptabilities of aroma and brightness were insignificantly different between NF and F10~30, while the mouth feel and overall acceptabilities were insignificantly distinct among all of the fermented teas. Therefore, these results suggest that the appropriate fermentation period for tea fermentation is 10 days. On the other hand, the total polyphenol and flavonoid content in the NF was the highest among all of the fermented teas. In the antioxidant parameters, EDA (electron donating ability), FRAP (ferric reducing antioxidant power), and LPOIA (lipid peroxidation inhibitory activity) in the NF were the highest among all fermented teas. Meanwhile, the XOI (xanthine oxidase inhibitory activity) was low, as well as insignificantly different from NF and F10~F30, whereas the AOI (aldehyde oxidase inhibitory activity) was markedly higher (38.09~41.70%) by the hot water tea extract (with or without fermentation), particularly the AOI that has increased via fermentation. In conclusion, the overall antioxidant activity tended to be reduced by fermentation; however, the EDA, FRAP and LPOIA in the fermented tea for 10 days was higher than the activities during 20~30 days of fermentation. There was a similar result in the color and acceptability of fermented tea for 10 days, which was remarkably better than those of 20-30 days. Therefore, fermented tea from the leaves of Smilax china L. could be expected to be used as a functional tea without the loss of inhibitory activity of both the XO and AO via fermentation.

• Korean Journal of Microbiology
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• v.34 no.3
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• pp.126-131
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• 1998

Reduction of hexavalent chromium to its trivalent form by leachate microorganisms was studied in batch and bench-scale continuous stirred tank reactor. The inoculum was a culture of microorganisms in leachate and capable of providing up to 90% chromate reduction during 72 h batch assay with $20mg\;Cr(VI)\;L^{-1}$ in minimal media containing different levels of leachate (10 to 60%) and glucose (50 to 200 mM). Addition of glucose increased the efficiency of chromate reduction, but adverse effect was observed with increase of leachate probably due to the competitive inhibition between chromate and sulfate ions. The continuous culture experiment was conducted for 124 days using synthetic feed containing different levels of chromate (5 to $65mg\;L^{-1}$) at room temperature. With a hydraulic retention time of 36 h, chromate reduction efficiency was mostly 100% when Cr(VI) concentrations in the reactor were in the range of 5 to $50mg\;L^{-1}$ Specific rate of Cr(VI) removal was calculated as $3.492mg\;g^{-1}\;protein\;h^{-1}$ during the period of 101~124 days from the start-up which showed 81.2% of average reduction efficiency. The results indicate the potential application of using leachate microorganisms for detoxification of hexavalent chromium in various chromium-contaminated wastewater from landfill or tannery sites.

• Microbiology and Biotechnology Letters
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• v.30 no.4
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• pp.395-401
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• 2002

Methyl ethyl ketone (MEK) and methyl isobutyl ketone (MIBK) have been widely used as solvents in various industries. Biodegradation of MEK and MIBK by Pseudomonas putida KT-3, which could utilize MEK or MIBK as a sole carbon source, was characterized, and the cosubstrate interaction in MEK/MIBK mixture was also studied. Within the range of initial MEK concentration (from 0.5 to 5.5 mM), an increased substrate concentration increased the specific degradation rate of MEK by P putida KT-3 (from 3.15 to 10.58 mmol/g DCW$\cdot$h), but the rate sightly increased at 11.0 mM of initial MEK concentation (11.28 mmol/g DCW$\cdot$h). The similar degradation rates of MIBK (4.69-4.92 mmol/g DCW$\cdot$h) were obtained at more than 3.0 mM of initial MIBK concentation. Kinetic analysis on the degradation of MEK/MIBK mixture by P. putida KT-3 showed that MEK or MIBK acted as a competitive inhibitor. Maximum degradation rate ($V_{max}$), saturation constant ($K_{m}$) and inhibition constant ($K_{1}$) were as follows: $V_{max,MEK}$=12.94 mmol/g DCW$\cdot$h; $K_{m,MEK}$=1.72 mmol/L; $K_{l,MEK}$=1.30 mmol/L; $V_{max,MIBK}$=5.00 mmol/g-DCW$\cdot$h; $K_{m,MIBK}$=0.42 mmol/L; $K_{l,MEK}$=0.77 mmol/L.

• Korean Journal of Poultry Science
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• v.37 no.3
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• pp.289-295
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• 2010

Because some zoonotic Salmonella can be transmitted to human through poultry products, threatening human public health, Salmonella infections in poultry are increasingly worldwide subject to control measures and programs. Given the fact that there are numerous opportunities for Salmonella to gain entry to extensive, integrated poultry operations including the hatching, handling, feeding, and processing facilities, the whole supply chain of poultry meat should be an object of Salmonella control programs as well as biosecurity of poultry farms. This article reviews Salmonella food poisoning caused by poultry source and critical need to control Salmonella in poultry productions, and describes practical strategies.

• Journal of Korean Society of Water and Wastewater
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• v.22 no.2
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• pp.187-193
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• 2008

Biological removal capacities for volatile organic compounds (VOCs) were determined using a yeast strain, Candida tropicalis. In this study, VOCs including toluene, benzene, p-xylene, and styrene as single substrates or mixtures were tested in the batch culture of the yeast strain. In addition, a kinetic model was applied to evaluate substrate interactions between the VOCs. The yeast strain was able to biodegrade each VOC effectively as a growth substrate, implying it could applied to wide range of VOCs. When the yeast strain was subjected to VOCs in mixtures, the biodegradation rate of one substrate were either increased (stimulated) or decreased (inhibited) by the presence of the others. Both benzene and toluene were inhibited by the other VOCs, and substrate interaction parameters estimated in the model indicated that styrene was the strongest inhibitor for the benzene and toluene biodegradation. Meanwhile, the biodegradation of p-xylene and styrene was stimulated by the presence of either benzene or toluene. The biodegradation rate of p-xylene was significantly increased especially by the presence of toluene, and the styrene biodegradation was enhanced greatly by the benzene addition. The results of the substrate interaction by the yeast strain suggest that the biodegradation rates for the VOCs in mixtures should be carefully evaluated. Furthermore, the competitive inhibition coefficient could be applied as a useful index to determine the substrate interaction

• Korean Journal of Microbiology
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• v.16 no.3
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• pp.122-130
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• 1978

During the sporulation stage in Saccharomyces cerevisiae J170, the incorporation of $D^{14}$ C-glucose into starved cells of sporulation stage as well as the vegetative one is appeared higher at pH 6.0. Glucose transport system, in both the vegetative and sporulation stage, is associated with "energy dependent" as the result of repression by such a respiratory inhibitor as 2, 4-dinitrophenol. The Km value of glucose uptake in vegetative stage and sporulation stage was 2.1 mM and 2.5 mM respectively, indicating that the glucose is considerably reuqired for vegetative growth. Competition and countertranspoer of glucose by frutose and galactose are more distinct in vegetative stage, comparing with sporulation stage. The main sugar components of yeast cells consists of ribose, mannose, and ${\alpha}, \;{\beta}-glucose$. Amounts of mannose is lower in the aporulation stage than that in the vegetative stage.

• Korean Journal of Microbiology
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• v.9 no.1
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• pp.39-45
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• 1971

During the sporulation stage in Saccharomyces cerevisiae J170, the incorporation of D$^{14}$ C-glucose into starved cells of sporulation stage as well as the vegetative one is appeared higher at pH 6.0. Glucose transport system, in both the vegetative and sporulation stage, is associated with "energy dependent" as the result of repression by such a respiratory inhibitor as 2,4-dinitrophenol. The Km value of glucose uptake in vegetative stage and sporulation stage was 2.1 mM and 2.5 mM respectively, indicating that the glucose is considerably reuqired for vegetative growth. Competition and countertranspoer of glucose by frutose and galactose are more distinct in vegetative stage, comparing with sporulation stage. The main sugar components of yeast cells consists of ribose, mannose, and .apha., .betha.-glucose. Amounts of mannose is lower in the aporulation stage than that in the vegetative stage.ive stage.

• Proceedings of the Korean Institute of Navigation and Port Research Conference
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• 2019.05a
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• pp.142-143
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• 2019

Busan Port ranked 6th in the world with 21.67 million TEUs of container handling in 2018, but the ship supply industry has fallen short of that. Despite its technological prowess, Korea's ship supply industry lacks competitive edge in many aspects such as government support, integrated platform, and infrastructure compared to overseas ship supply industries. The use of code, which is not standardized, can be cited as a leading factor that undermines the competitiveness of Korea's ship supply industries. In the ship supply industry, the use of non-standardized codes can make it difficult to manage or analyze meaningful statistics, and, by extension, can lead to the loss of new business opportunities. Therefore, in this study, we intend to use local ship supply transaction data to study how to standardize item code to solve the problem.

• Proceedings of the Korea Association of Information Systems Conference
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• 2004.11a
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• pp.349-365
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• 2004

기업의 또는 부문에서 구축된 각 정보시스템들은 시간이 지남에 따라 기업의 경쟁우위를 확보하기 위해 통합의 필요성이 증대하게 되었는데, 이러한 필요에 의해 제기된 것이 ERP(Enterprise Resource Planning: 전사적 자원관리)이다. 급변하는 기업의 내${\cdot}$외부 환경에 대해 신속하게 대응하기 위해 ERP 시스템을 도입하는 기업들의 수가 증가함에도 불구하고 ERP 원가관리시스템에 대한 연구는 아직까지 그 범위가 한정되었다고 할 수 있다. 본 논문은 ERP 도입 현황 및 원가관리시스템의 도입${\cdot}$설계현황자료를 바탕으로 하여, 중소기업의 ERP 원가관리시스템의 성공적 도입을 위한 방향을 제시하고자 한다. 중소기업에서 ERP 원가관리시스템을 도입할 때는, 원가관리시스템의 특성과 구축 목표, 구조 설계, 원가대상 설정 등과 관련된 다음과 같은 사항들을 고려하여야 성공적인 시스템을 구축할 수 있을 것이다. 첫째, ERP 원가관리시스템 특성 분석단계에서는 원가정보를 구성하는 내용의 충실성뿐만 아니라 정보가 전달${\cdot}$제공되는 범위와 대상의 적합성과 함께 그 표현의 형식 또한 고려되어야 한다. 둘째, ERP 원가관리시스템 구축목표 설정단계에서는 인가관리정보의 산출요건에 대한 명확한 이해와 목표설정을 기반으로 해야 한다. 셋째, ERP 원가 관리시스템 구조 분석 및 선계단계에서는 생산관리시스템 및 원가대상 설정 분석이 이루어져야 한다. 넷째, ERP 원가관리시스템 구현단계에서는 원가관리시스템과 타 계열시스템과의 인터페이스를 고려해야 한다. 따라서 원가관리시스템의 구현 시에는 관련시스템에서 어떠한 정보론 인터페이스 받을 것인가를 명확히 하여 시스템 가동 시에 타 관련시스템과 원활한 연계가 되도록 함으로써 전사적 종합시스템이 되도록 하여야 학 것이다.RS와 제진장치에 대한 전체적인 성능평가를 성공적으로 수행하였으며, 운전결과 및 경험은 향후 상용설비를 위한 기본자료로 활용할 것이다.X>, 그리고 입원기간은 $21.6\pm14.3일(13\~56)$이었다. 수술 후 평균 CK-MB는 $11.3\pm14.1ng/mL$였다. 수술 후 조기 혈관 개존율은 $100\% (24/24)$였다. 모든 환자에서 완전 추적이 가능하였으며 평균 추적기간은 $20.4\pm15.2개월(5\~43)$이었다. 이 기간 중 사망환자나 흉통이 재발한 환자는 없었다. 걸론: 80세 이상 고령의 환자에서 OPCAB은 수술 후 합병증을 줄이고 좋은 결과를 보여 주었다. 그러므로 고령의 환자에서도 관상동맥우회술의 적응증이 되면 적극적으로 수술을 시행할 필요가 있으며, 수술방법은 OPCAB이 좋을 것으로 생각한다서 실용적 개발의 가능성을 보였다.에 따라 현저한 차이가 있었으며 Dimethoate처리$(30^{\circ}C,\; 0.2\%$액에서 24시간)에 의하여 볍씨의 호흡량이 감소되었다. 9) 산소호흡량과 평균발아소요일수와는 $\gamma=-0.945$로 부의 유의한 상관을 보였는데 산소호흡량이 많은 품종은 평균발아소요일수가 짧은 경향을 보였다. 10) 볍씨의 산소호흡량과 Dimethoate 처리에 의한 볍씨의 발아저해도와는 $\gamma=-0,771$의 높은 부의 상관을 보였으며 산색호흡량이 많은 품종이 발아저해도가 낮고 적은 품종에서는 높았다. 현재까지는 그 활동이 11.2년의 주기성을 보여주지만 그 이전에 있어서는 그 활동이 극히 약화되었을 뿐만 아니라 매우 불규칙하다는 것이 Schneider와 Mass(1975)에 의해 밝혀졌다. 결국 1710년대부터 현재까지 우리나라에 있어서 벼멸구와 흰

• Korean Journal of Construction Engineering and Management
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• v.8 no.6
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• pp.159-166
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• 2007

Work delay is one of the facts that make the reliability of construction projects decrease. Therefore, it is important to classify and prioritize the delay factors. This research analyzed key delay factors in apartment house construction through survey. The results of analysis are as follows. (1) Insufficient work force is the key delay factor in structural and finish work. (2) Improper craft of worker is the key delay factor in electrical work. (3) Incompletion of proceeding work is the key delay factor in mechanical work.