구조 건전도 모니터링 시스템과 응답기반모드해석 기법의 발전과 함께 토목구조물의 고유진동수나 감쇠비, 모드형상과 같은 동특성의 변화를 통해 구조물의 상태를 평가하거나 손상도를 추정하는 연구가 지속적으로 수행되었다. 그러나 온도나 풍속, 진폭 같은 환경 및 거동조건에 따른 동특성의 변동성으로 인해 구조물의 손상이나 상태 변화에 의한 영향만을 파악하는 데 한계점이 있다. 본 연구에서는 복잡한 공기역학적 특성을 보이는 장대교량의 동특성과 환경 및 거동조건 사이의 상관성을 분석하기 위한 다중선형회귀분석 기반의 예측모델을 제안하였다. 응답기반모드해석 기법을 적용하여 3달간의 계측데이터로부터 대상 구조물의 고유진동수와 감쇠 비를 추정하고 온도나 풍속, 구조물의 진폭 등 환경 및 거동조건과의 다중선형회귀분석을 통해 각 요인의 변화가 동특성의 변동성에 미치는 영향을 정량화하였다. 또한, 랜덤 추출한 80%의 데이터를 토대로 다변수 회귀모델을 구축하고 나머지 20% 데이터의 환경 및 거동조건으로부터 예측한 값과 실제 추정치를 비교함으로써 제안한 모델의 예측 성능을 검증하였다. 마지막으로 단계적 회귀분석을 통해 기여도가 높은 독립변수를 파악하고 예측 성능을 개선하였다.

The emission of odor, characterized by the combustion conditions and biomass types resulting from the use of a biomass incinerator, was analyzed. The following biomass types were considered: bark, board waste, sawdust, wood flour, wood fiver, wastewater sludge, and timber wastewater. As a study method, the physico-chemical characteristics of each biomass type were analyzed to predict the potential substances that might be emited under incomplete combustion conditions. And, the emission components of odor emission by biomass were analyzed at the laboratory level using a combustion device. In addition, the characteristics of the contaminant (odor) emission per mixture ratio of biomass were analyzed in a stoker incinerator that is in operation in an actual establishment at a scale of 300 ton/day. In the biomass emission experiment using the combustion device at the laboratory level, the major substances such as Acetic acid, Styrene, Toluene, Benzene, Dichloromethane, etc. were analyzed, and these components were determined to increase odor index. VOCs measurement in the outlet of the stoker incinerator indicated that Acetaldehyde, Ethanol, Acetonitrile, Ethyl acetate, Toluene, etc. were detected as the major substances. These were similar to the emission substances presented by the experiment that had investigated emissions by biomass type. A study on the Effect of Operational Conditions in biomass stocker incinerator on the concentration of odorous materials emitted from stack showed a close relationship between the input by biomass type and urea, temperature in the incinerator, and the tendency to emit/produce odor.

This study was performed to evaluate the drying characteristics of food waste in oil vacuum evaporation system withdrying conditions and composition of food waste. The food waste was collected and separated into 4 categories such asvegetables, fruits, grain (rice), meats and others. which composition were 41.9%, 26.7%, 2.8%, 25.5% and 0.4%,respectively. Each food waste separated was dried and compared its characteristics in the same condition of vacuumpressure (−450mmHg), temperature (110oC) and mixing ratio (oil:food waste=1:1) for 90min of drying period. Theexperimental results showed that the moisture contents of dried vegetables, fruits and meats were less than 10%. Howeverthe grain was hard to be dried which moisture content was much high as 24.5%. This high value of the grain was thoughtdue to the viscosity of grain which prohibit oil penetration and water vaporization during drying process. In order tocompare drying characteristics with operating parameters, vacuum pressure, temperature and mixing oil type were changed.The operating temperature and vacuum pressure were major sensitive parameters. As the temperature increase and thepressure lower, the drying rate of food waste was increased and its efficiency was also improved. Especially, the moisturecontent of dried food waste was lower than 5% which was satisfied SRF standard 10% at the temperature over 110oC.Compared the effect of mixing oil type, waste cooking oil was more effective than refined oil in viewpoint of dryingefficiency. However, there is no difference of drying efficiency between fresh and waste cooking oil.

Electrochemical reductive extraction of tin from semiconductor plating process wastewater was experimented using synthetic wastewater. Copper and graphite plate were used as a cathode and an anode, respectively. The tin extraction could be optimized in pH 0.5 and polar space of 60 mm. The extraction rate of tin per minute was increased as current and initial tin concentration increased, and more than 87% and 97% of tin could be extracted within 80 minutes at 500 mg/L and 1,000 mg/L of initial tin concentration, respectively. The electrochemical reaction orders and kinetic coefficients were 1.24 ~ 1.26 and 0.004 ~ 0.006 (L/mg)(n − 1)min−1. The residual concentration of tin could be expressed as Ct= (Co −0.246+ 0.0012t)−4.065.