• 한국지구과학회:학술대회논문집
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• 2003.09a
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• pp.112-125
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• 2003

구름의 몬순의 활동에 있어서 직접적으로나 간접적으로 영향을 준다. 본 연구에서는 이러한 구름이 몬순의 활동에 어떠한 영향을 주는지를 알아보기 위해 ISCCP 구름자료와 GAME 재분석 자료를 입력자료로한 장파 복사 모델을 수행하였다. 모델 수행의 결과로 얻어진 대기 상부에서의 플럭스는 CERES 관측치와 비교하였으며, 구름에 의한 가열율은 몬순활동을 해석하기 위해 사용하였다. 구름이 몬순에 끼치는 영향을 파악하기 위해 맑은 대기의 가열율과 구름을 포함한 평균 대기의 가열율의 차이를 구하였으며, 이를 수평과 연직분포의 관점에서 해석하였다. 가열율의 지리적 분포는 수평적으로는 인도양에서 장파 복사 가열율의 최대가 나타났으며, 가열의 최저 (냉각)은 티벳고원에 나타났다. 이러한 공간적 분포는 구름이 남북방향으로 차등가열을 유발시키고 있음을 보여주고 있어 구름의 분포가 열적인 몬순순환을 강화시켜주고 있음을 시사하고 있다. 이러한 차등가열의 강화는 동서방향으로도 나타나 구름이 동서방향 순환에도 영향을 줄 수 있음을 보여준다. 구름에 의한 복사 가열의 연직구조는 운정에 의한 냉각과 운저에 의한 가열이 일어날 수 있음을 보여주고 있으며, 이로 인해 대기의 불안정성이 높아져 연직 운동을 향상시킬 수 있는 역할을 하고 있음이 밝혀졌다. 즉 몬순순환에 의해 생성된 구름은 구름 생성의 원인이 되었던 순환을 더욱 강화시키고 있음을 보이고 있다.

• 한국생물공학회:학술대회논문집
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• 2000.11a
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• pp.216-219
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• 2000

Pyrolysis products of woody biomass were consistedofvarious linear hydrocarbon, aromatics or condensed cyclic compounds. In order to obtain biomass pyrolysis products, more equipments and time were needed. But solvolysis of woody biomass with acetone easily obtained decomposition products and enhanced conversion rate(18.72%, max.) from woody biomass than pyrolysis of woody biomass. Beacause solvolysis with acetone improved conversion rate (26.64%, max.) of lignin. the whole conversion rate was improved. But above $300^{\circ}C$, lignin showed lower conversion rate, so the whole conversion rate decreased. Solvolysis products of woody biomass with acetone were same as pyrolysis products. Above $400^{\circ}C$, methoxy phenols were completely disappeared.

• KSBB Journal
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• v.5 no.1
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• pp.59-67
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• 1990

Enzymatic hydrolysis of insoluble cellulose was performed in a bubble column with tangential flow ulrafiltration membrane unit. The reactor was operated in a batch mode as well as semi-continuous and continuous with continuous removal of products through the tangential flow ultrafiltration membrane. The optimum superficial gas velocity was 1-3cm / sec so as to avoid bubble coalescence and enzyme denaturation. In continuous and selni-cotinuous process, the conversion was gradually increased but the total reduced sugar concentration was drcastically dereased with the dilution rate. It was concluded that the bubble column attaching tangential flow ultrafiltration membrane unit was effective on continuous hydrolysis of cellulose and recovery of enzyme.

• Journal of Korean Society of Environmental Engineers
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• v.28 no.1
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• pp.61-66
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• 2006

The combined ADEPT(Anaerobic Digestion Elutriated Phased Treatment)-SHARON(Single reactor system for High Ammonium Removal Over nitrite)-ANAMMOX(Anaerobic ammonium oxidation) processes were operated for resources recovery and nitrogen removal from slurry-type piggery waste. The ADEPT process operated at an acidogenic loading rates of 3.95 gSCOD/L-day, the SCOD elutriation rate and acid production rate were 5.3 gSCOD/L-day and 3.3 gVFAs(as COD)/L-day, respectively. VS reduction and SCOD reduction by the hydrolysis were 13% and 0.19 $gSCOD_{prod.}/gVS_{feeding}$, respcetively. Also, the acid production rate was 0.80 $gVFAs/gSCOD_{prod}$. In methanogenic reactor, the gas production rate and methane content were 2.8 L/day($0.3m^3CH_4/kgCOD_{removal}@STP$) and 77%, respectively. With these operating condition, the removals of nitrogen and phosphorus were 94.1% as $NH_4-N$(86.5% as TKN) and 87.3% as T-P respectively.

• Journal of Korean Society of Environmental Engineers
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• v.31 no.5
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• pp.378-381
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• 2009

The purpose of this research is the evaluation of removal efficiency of THMFP in BAC. The changes of four types of THMFP and total THMFP were examined in the influent and effluent of BAC filter from March to December in 2008. It turned out that the amounts of brominated THMFP were obviously higher in winter and autumn compared to the spring and summer, which also resulted in an increase of the total-THMFP levels during winter and autumn. In addition, long-term running of BAC filter shows the good removal function of chloroform formation potential, but not brominated THMFP; with further bromination, this function was declined, as it shows the formation of bromoform in BAC filter during October and December. These results were caused by changing of the proportion of $Br^-$/DOC.

• Journal of Convergence Society for SMB
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• v.2 no.2
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• pp.1-6
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• 2012

In this paper, we propose a detector generation model which is applied to immune system to improve the misuse detection rates in misuse detection models. 10cv method is used to sendmail data which is provided by the DARPA. We experimented and analyzed the misuse detection rate that is either judgment of the normal system call as abnormal system call or judgment of the abnormal system call as normal system call. In the experiment, between detector which was generated by any abnormal system call and temporary detector. I did experiments with a new detector which was removed temporary detector which made a wrong decision for normal system call as an abnormal system call and abnormal system call as a normal system call. The misuse detection rate of detector which is applied to the immune system is greater than the other detector by 0.3%.

• Culinary science and hospitality research
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• v.18 no.4
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• pp.266-276
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• 2012

Salt, one of the main ingredients to make bread, functions differently according to environmental changes such as usage levels and methods. We examined the effects of yeast soaking time in about 8% salt solution on gas production and fermentation rate of dough and characteristics of white bread. Gas retention, related to gas production and fermentation rate, was the best at the 45 min soaking time. And pH of dough was appropriate to the fermentation in the range of 15 to 45 min of soaking time. Volume and specific volume of bread were best in 45 min soaking time(p<0.001), but the hardness of crumb texture analyzed with TA was the hardest among the samples(p<0.001). Brightness of color(L value) was significantly affected by soaking time(p<0.001), but b value was not considered. According to the preference test, the white pan bread made with 45 min soaking time in salt solution was preferred the most.

• Resources Recycling
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• v.30 no.6
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• pp.12-18
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• 2021

The water-gas shift reaction is the subsequent step using steam for hydrogen enrichment and H₂/CO ratio-controlled syngas from gasification. In this study, a water-gas shift reaction was performed using syngas from an RPF gasification system. The water-gas shift using a catalyst was performed in a laboratory-scale tube reactor with a high temperature shift (HTS) and a low temperature shift (LTS). The effects of the reaction temperature, steam/carbon ratio, and flow rate on H₂ production and CO conversion were investigated. The operating temperature was 250-400℃ for the HTS system and 190-220℃ for the LTS system. Steam/carbon ratios were between 1.5 and 3.5, and the composition of reactant was CO : 40 vol%, H₂ : 25 vol%, and CO₂ : 25 vol%. The CO conversion and H₂ production increased as the reaction temperature and steam/carbon ratio increased. The CO conversion and H₂ production decreased as the flow rate increased due to reduced retention time in the catalyst bed.

• Journal of the Korea Organic Resources Recycling Association
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• v.17 no.1
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• pp.49-57
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• 2009

This research examined the effect of ammonia nitrogen loading rate(NVLR) on the anaerobic digestion of slurry-typed swine wastewater. The anaerobic reactor was used an upflow anaerobic sludge blanket (UASB) process. This UASB reactor was operated at a NVLR of $0.02{\sim}0.96kg{NH_4}^+-N/m^3/day$. The methane content showed the range of 73.3~77.9% during the steady state period. Free ammonia(FA) concentration increased over inhibition level as pH increase from 7.3 to 8.2. However, in consideration of methane content, methane producing bacteria (MPB) inhibition by FA and total ammonia(TA) was not observed. A stepwise increase of the NVLR resulted in a deterioration in the COD removal rate in UASB reactor. The COD removal rate were 60% for NVLR up to $0.55kg{NH_4}^+-N/m^3/day$. As the NVLR increased from 0.09 to $0.96kg{NH_4}^+-N/m^3/day$, the biogas production rate varied from 3.71 to 9.14L/d and the methane conversion rate of the COD varied from 0.32 to $0.20m^3CH_4/kg$ COD removed. Consequently, in considerations of FA concentration, COD removal rate, and $CH_4$ production rate, the UASB reactor must be operated to lower than $0.40kg{NH_4}^+-N/m^3/day$ of NVLR.

• Applied Biological Chemistry
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• v.30 no.4
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• pp.311-314
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• 1987

High-level yeast inocula was investigated as a means of overcoming the inhibition problem in ethanol fermentation of hemicellulose hydrolyzate. When the inoculum exceeded 25g dry cells/liter, the fermentation proceeded completely to the end within 24 hours. Furfural was taken up by Pachysolen tannophilus and catabolized to furfuryl alcohol. Thus inhibitory effect of furfural component was less adverse toward ethanol production than that of non-furfural components in hemicellulose hydrolyzate. The specific ethanol productivity in the fermentation of hemicellulose hydrolyzate was 14% of that of simulated media containing 41.8g xylose and 2.3g furfural per liter.