• 전력전자학회:학술대회논문집
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• 전력전자학회 2001년도 전력전자학술대회 논문집
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• pp.172-176
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• 2001

In this paper, a new detection algorithm of faulted voltages under the unbalanced condition and a control algorithm of the instantaneous voltage sag corrector (IVSC) are proposed. To quantify the unbalance under fault conditions, the voltages are decomposed into two balanced three-phase systems using the symmetrical components of positive and negative sequence voltages, which is defined by magnitude factor (MF) and unbalance factor (UF). New control algorithm based on MF and UF values for instantaneous voltage compensation are proposed and verified through the PSCAD/EMTDC simulation and experimental results.

• Restorative Dentistry and Endodontics
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• 제27권4호
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• pp.411-420
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• 2002

The aim of this study is to compare the adaptability of thermoplasticized injectable gutta-percha technique to the canal walls in ribbon-shaped canals. Thirty resin models simulated ribbon-shape canals were instrumented to #40 using .06 taper Profile systems. Three groups of each 10 resin models were obturated by the lateral condensation technique(LC) and the two thermoplasticized injectable gutta-percha technique; Ultrafil Endoset+Obtura II(EO) and Ultrafil Firmset(UF), respectively. After resin model were kept at room temperature for 4 days, they were resected horizontally with micro-tome at 1, 2, 3, 4 and 5mm levels from apex. At each levels. image of resected surface were taken using CCD camera under a stereomicroscope at $\times$40 magnification and stored. Ratio of the area of gutta-percha was obtained by calculating area of gutta-percha cone to the total area of canal using digitized image-ana-Iyzing program. The data were collected then analyzed statistically using One-way ANOVA. The results were as follows. 1 At 1mm levels, there was no statistically significant difference in the mean ratio of gutta-percha among the groups. 2. At 2mm level, EO showed the highest mean ratio of gutta-percha (p<0.05) and there was no significant difference between LC and UF. 3. At 3, 4, 5mm levels, EO and UF had significantly greater mean ratio of gutta-percha than LC(p<0.05) and there was no significant difference between EO and UF. In conclusion, the thermoplasticized injectable gutta-percha techniques demonstrated relatively favorable adaptability to canal walls than lateral condensation technique in ribbon-shaped canals except for 1mm level.

• 한국해양공학회지
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• 제23권5호
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• pp.71-78
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• 2009

In ship design or offshore structure design, the evaluation of buckling strength (or ultimate strength) is critical to the determination of scantling of stiffened plates. For this reason, it is useful to study the effect of applying different formula or the relationship between stiffened plate with buckling utilization factor (UF). It can facilitate a designer to decide how much the scantling should be reinforced or how much can be reduced for an optimal design. This paper conducts a comparative study for three buckling check methods; DNV-Ship-Rule, DNV-RP-C201, DNV-PULS. The capacity curves and 2D contour plot for utilization factors versus bi-axial in-plane stresses are compared. The contour plots of DNV-Ship-Rule and DNV-PULS show smoothly increasing trends of UF as the applied in-plane stresses increase, however that of DNV-RP-C201 shows rapidly increasing trend as the applied stresses go beyond transverse buckling stress. A sensitivity analysis is performed to investigate the influence level of each parameter of a stiffened plate on UF. Resulting from the analysis, plate thickness is identified to be the most affective parameter to UF regardless of the buckling check methods. Based on the addressed study, optimal designs for bottom plate of 165 K tanker corresponding to three formulas are compared with each other. DNV-PULS yields 1 mm and 2 mm less thickness than DNV-Ship-Rule and DNV-RP-C201, respectively.

• 청정기술
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• 제12권3호
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• pp.151-156
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• 2006

염색폐수 처리를 위해 세라믹 정밀여과막 (MF)과 고분자 한외여과막 (UF)의 복합공정을 적용, 색도 및 유기물 (TOC) 제거율을 통해 공정을 최적화하고, 염색폐수의 분리효율을 조사하였다. 막 회복을 통한 운전 효율향상을 위해 역세척과 화학세정을 수행한 결과, 역세척에 의한 정밀여과막은 2분 주기로 1초 동안 역세척하였을때 투과수량이 10.3% 증가하였고, 한외여과막은 0.1% 수산화나트륨 용액으로 화학세정하였을 때 97%의 회복률을 나타내었다. 이때, 유기물, 색도, 부유물질(SS)의 제거율은 각각 84.6%, 97.4% 및 100%를 나타내었다. 분 복합공정의 적용은 염색폐수의 색도와 유기물 제거에 효과적임을 확인할 수 있었다.

• 한국물환경학회지
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• 제18권4호
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• pp.387-394
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• 2002

본 연구는 $TiO_2$ 광촉매 및 응집-여과-중화공정을 거친 아크릴폐수를 UF(tubular)/RO(spiral wound)공정에 적용하여 적용압력과 온도변화에 따른 성능변화를 고찰하였다. 한외여과 관형모듈에서 광촉매 전처리수와 응집-여과-중화 전처리수의 COD, T-N은 온도 및 압력변화에 크게 영향을 받지 않고, 제거효율도 낮은 것으로 확인할 수 있었다. TDS 및 turbidity의 경우 한외여과 관형 모듈에서 광촉매 전처리수가 응집-여과-중화공정의 처리수에 비해 처리효율이 우수함을 확인하였다. T-N, TDS는 역삼투막 공정에서 우수한 제거효율을 나타내었다.

• 대한환경공학회지
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• 제27권8호
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• pp.892-899
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• 2005

지하수는 지표수에 비하여 수질이 양호하며 외부로부터의 오염원이 적은 편이다. 하지만 현재 우리나라의 지하수도 산업화, 도시화에 의하여 많은 오염이 발생되고 있다. 그 중에서도 PCE와 TCE는 난분해성 염소계 유기화합물로서 그 처리에 신중을 기해야 한다. 본 연구에서는 PAC-막분리 공정을 적용하여 이들 물질을 보다 효과적이면서 컴팩트하게 처리할 수 있었다. 막의 재질에 따른 효율의 차이는 별로 없었으며, PAC가 투과 플럭스의 저하를 유발하지는 않았다. 따라서 PAC의 주입이 효과적으로 이루어진다면 막에서 발생하는 오염을 줄여줄 수가 있으며 보다 효율적인 운전이 이루어 질 수가 있다.

• The Plant Pathology Journal
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• 제32권6호
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• pp.528-536
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• 2016

Although many fungicides are registered for use to control powdery mildew on cucurbits, management of resistance to fungicides in pathogen populations still remains a major challenge. Two biopesticides Regalia SC and HMO 736 were evaluated in the greenhouse and field for their efficacy against powdery mildew in squash. In greenhouses, Regalia SC alone significantly (P < 0.05) reduced powdery mildew compared to the nontreated control, and was as effective as the chemical standard Procure 480SC (triflumizole). In alternation with Procure 480SC, Regalia SC demonstrated greater or equivalent effects on reducing the disease. HMO 736 alone showed varying levels of disease control, but alternating with Procure 480SC significantly improved control efficacy. In addition, application of Regalia SC or HMO 736 each in alternation with Procure 480SC significantly increased the chlorophyll content in leaves and the total fresh weight of squash plants, when compared with the water control, Regalia SC and HMO 736 alone. In field trials, application of Regalia SC and HMO 736 each alone significantly reduced disease severity in one of two field trials during the early stage of disease development, but not during later stages when disease pressure became high. Both Regalia SC and HMO 736 each applied in alternation with Procure 480SC significantly improved the control efficacy compared to Procure 480SC alone. Results from this study demonstrated that an integrated management program can be developed for powdery mildew in squash by integrating the biopesticides Regalia SC, HMO 736 with the chemical fungicide Procure 480SC.

• 동의생리병리학회지
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• 제22권2호
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• pp.365-370
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• 2008

This study was performed to investigate the influence of extracts from mixed culture with Tricholoma matsutake mycelium and Cordyceps militaris mycelium on hypoglycemia in streptozotocin-induced diabetic rats. Experimental animals were divided into 7 groups : normal control group(NC), diabetes control group (DC), positive control group(PC), non-fermented OCM(oriental medicine & cereal medium) extracts group (UM), crude polysaccharide of non-fermented OCM extracts group (UME), fermented OCM extracts group (UF), crude polysaccharide of fermented OCM extracts group (UFE). NC, DC groups were orally administered saline, PC group was orally administered acarbose. UM, UME, UF, UFE groups were orally administered each extract once a day for 14days. Blood glucose level was lower in the all administering OCM extract groups (UM, UME, UF, UFE) than in the diabetes group(p<0.05), and specially UF, UFE groups were similar to tendency of PC group. ALT, ALP activity in OCM groups were not significantly lowered than PC group(p<0.05). AST activity was not different with PC group. The results of this study show that extracts from mixed culture with Tricholoma matsutake mycelium and Cordyceps militaris mycelium may have a beneficial effect on the hypoglycemia.

• Journal of the Korean Wood Science and Technology
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• 제33권2호통권130호
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• pp.29-39
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• 2005

Formaldehyde emissions from wood-based panels bonded with pine and wattle tannin-based adhesives, urea-formaldehyde resin (UF), melamine-formaldehyde resin (MF), and co-polycondensed resin of urea-melamine-formaldehyde (UMF) were measured by the Japanese standard method using a desiccator (JIS A 1460) and the EN 120 (European Committee For Standardization, 1991) method using the perforator value. In formaldehyde emission, all particleboards made using the wattle tannin-based adhesive with three different hardeners, paraformaldehyde, hexamethylenetetramine, and tris(hydroxyl)nitromethan (TN), satisfied the requirements of grade $E_1$. But only those made using the pine tannin-based adhesive with the hexamine as hardener met the grade $E_1$ requirements. Hexamine was effective in reducing formaldehyde emission in tannin-based adhesives when used as the hardener. While the UF resin showed a desiccator value of $7.1mg/{\ell}$ and a perforator value of 12.1 mg/100 g, the MF resin exhibited a desiccator value of $0.6mg/{\ell}$ and a perforator value of 2.9 mg/100 g. According to the Japanese Industrial Standard and the European Standard, the formaldehyde emission level of the MDF panels made with UF resin in this study came under grade $E_2$. The formaldehyde emission level was dramatically reduced by the addition of MF resin. The desiccator and perforator methods produced proportionally equivalent results. Gas chromatography, a more sensitive and advanced method, was also used. The samples for gas chromatography were gathered during the experiment involving the perforator method. The formaldehyde contents measured by gas chromatography were directly proportional to the perforator values.

• 상하수도학회지
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• 제18권6호
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• pp.770-777
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• 2004

Three pilot-scale membrane systems were operated using lake water as influent in this study. Microfiltration (MF) membrane with pore size of 0.01 m was used in Systen I of which filtration mode was set at constant pressure of $1kgf/cm^2$. Ultrafiltration (UF) membranes with molecular cutoff (MWCO) of 80,000 and 13,000 were used in System II-1 and II-2, respectively. Constant flow mode was applied at the range between 0.7 and $1.5m^3/m^2{\cdot}d$ (average of $1.1m^3/m^2${\cdot}d) for System II-1 and between 0.37 and $1.65m^3/m^2{\cdot}d$ (average of $1.18m^3/m^2{\cdot}d$) for System II-2. In System I, the flux changed from $1m^3/m^2{\cdot}d$ to $0.2m^3/m^2{\cdot}d$ during the operation time of 5 months. System II showed recovery of 94% under the allowable maximum pressure of $3kgf/cm^2$ during the same operation period. From these results, the efficient operation was observed in constant flow mode with respect to filtration time and recovery. Average filtrate turbidity showed 0.0071 NTU in System I and 0.0054 NTU in System II, which implied that high turbidity removal was obtained in both MF and UF systems with no significant difference between MF and UF. From the fact that membrane flux depends largely on membrane type and operation mode, a guideline of optimum design and operation should be suggested for application of membrane systems to full scale water treatment.