국가 주도로 2009년부터 개발중인 경수로 사용후핵연료 건식저장시스템은 금속 겸용용기와 콘크리트 저장용기의 두 가지 방식이다. 국외 건식저장시설 운영 시 주요 격납감시 방안으로는 금속 겸용용기인 경우 이중 뚜껑 사이에 압력센서를 설치 하여 실시간 압력변화를 감시하는 방법이 있고 콘크리트 저장용기의 경우는 캐니스터 기반으로 주요 격납 경계인 뚜껑을 이중으로 용접하는 방식으로 구조물(over pack 또는 module)의 공기 유로인 입구 및 출구에 대한 온도 변화를 감시하는 방 법으로 격납을 관리하는 것으로 나타났다. 미국, 독일 등 30 년 이상 안정적으로 저장시설을 관리한 국가의 다양한 적용기 술 및 운영사례를 조사/분석하여 우리가 개발중인 저장시스템에 적용할 수 있는 격납감시 방안을 도출하는데 활용할 수 있 도록 하였다.

This study aims to examine the light weight impact sound insulation of dry type system in apartment house. To achieve this goal, sounds which have same loudness according to rating methods were suggested to subjects. And followings are results. 1) The measurement frequency level average of dry type system-on is more suitable than that of dry type system-off which are dependent on specific frequency for light-weight floor impact sound. 2) Level average for measurement frequency of 100∼ｾ500Hz is more correspondent to vibration-acoustic response than that of measurement frequency of 100∼!500Hz which is for KS F 2863-2, existing rating method.

The effect of major operating parameters in spray drying sorber(=SDS) for automatic control for the simultaneous removal of acidic and organic gaseous pollutants from solid waste incinerator was performed. The field experiment was carried out in pilot scale test for the quantification of major operating parameters of hydrophilic and the hydrophobic pollutants. The removal efficiencies of SO2 and HCI in the 5wt% slurry condition were being increased with the increase of the stoichiometric ratio which is the molecular ratio of lime to the pollutant concentration, and with the decrease of inflow flue gas temperature in the pilot SDS reactor. The removal efficiency along the height of spray drying sorber was closely related to the temperature profile, and more than 90% of total removal efficiency was achieved in an absorption region. For the removal of acidic gas the optimum operating condition considering the economics and a stable operation is the 5wt% of slurry concentration, 1.2 of stoichiometric ratio and 250℃ of inflow flue gas temperature. For the organic gases of benzene and toluene the removal efficiencies were 20 - 60% which is much lower than that of acidic gas. The best removal efficiency was obtained at 1.5 of stoichiometric ratio and 250℃ of inflow flue gas temperature. The organic's removal efficiency along the height of spray drying sorber was quite different from that of acidic gas, that is, more than 60% of the total removal efficiency for benzene and 90% of the total removal for toluene were achieved in the dried adsorption region, which was formed at the lower or exit part of the reactor.