The first Pagoda of Korea was introduced from China, and adapted from the wooden multi-storied pavilion. Also in Bronze one, multi-storied type of wooden pagoda was adapted. Bronze pagoda was used to buddhist ossuary and a kind of metalwork. Metalworks were made of gold, silver, copper, or iron by one of the methods of production-casting or hammering and decorated design of incision, raise, openwork, gold- plating or inlaying with gold and silver. Sometimes it was used as the easy carriage of Buddha image by guess. In most cases, the plan of Bronze pagoda was square and podium was one story. but in the advance of podium two-storied platform appeared. Column appeared in a symbol, so it didn't appear in a square and circular form. It means that the column was vertical member which only divided the wall. In koryo period, Gabled roof and Half-hipped roof was spreaded in public but Bronze pagoda was used to square Hipped roof. Vertical shaft over roof(上輪部), apart from body of pagoda(塔身部), was inserted on the hole above the Bokbal(覆鉢) for the balance of pagoda. And a thick iron bar put in the roof to the platform. It was sustained the balance of pagoda. The stories of pagoda were various from 3rd stories to 9, the lower stories was larger scale and the higher was smaller one.

야온과 시용질소의 형태를 달리한 양액이 탑채와 백경채의 생육 및 품질에 미치는 영향을 알아보기 위하여 실시한 실험의 결과는 다음과 같다. 1. 탑채, 백경채 모두 야온 15℃ 에서 생육이 왕성하여 생체중이 무거웠으나 건물율과 vitamin C의 함량은 온도가 낮아질수록 증가하였다. 2. 양액의 N형태 비율에 따른 백경채의 생육은 NO3- : NH4+ 의 비가 0 : 8에서만 극히 생육이 저조하고, 다른 처리구에서는 큰 차이가 없었다. 3. 양액내 NO3--N의 함량이 높을수록 vitamin C의 함량이 많고, NH4+-N의 함량이 높을 때는 건물율이 높았다.

In order to investigate the extraction mechanism of barley tea in cylindrical packed column, pilot plant scale packed column was designed and constructed. And extraction conditions for steady flow in the packed column were searched. The main results of this study are as follows : 1. Circulation of the stock barley tea before the extraction running was indispensable in consideration of inequality, gas, particles existed in packed bed. Solid-liquid equilibrium was initially maintained after the circulation. 2. Flow direction of solvent must be up-flow for maintaining the constant bed height and flow rate during the extraction. Paessure drop in pucked bed was similar to decrease ratio of extract concentration. 3. The porosity of packed bed was in the range of 0.24∼0.36 according to the particle size. And it was decreased as the particle size became smaller.

In this paper, a tuned mass damper is applied to improve the seismic performance of the lighting tower. The light tower has a high slenderness ratio, low lateral stiffness and top mass is large structure so this has weak for vibration characteristics. The optimized damping coefficient and stiffness were applied to the four lighting tower models analyzed. As a result, the light tower with TMD showed a tendency to reduce the displacement response significantly against the earthquake.

The aim of this paper is to compare the characteristics of the T-P removal from synthesized municipal wastewater by electro-coagulation using cylindrical Al and Fe electrode as anode. For this purpose, a concentric circle type electrolysis reactor was used and the operating conditions for T-P removal from synthesized wastewater are as follows; potential 10 V, electrolyte 0.03% NaCl, initial T-P concentration 1.0 ~ 6.0 mg/L and flow rate 1.0 ~ 5.0 L/min. From the experimental results, T-P concentration of treated wastewater was decreased to less than 0.2 mg/L enough to discharge standard and Al electrode showed performance than Fe electrode for T-P removal by electro-coagulation. Optimal conditions for T-P removal to less than 0.15 mg/L which is 75% of discharge standard for large scale municipal wastewater plant (capacity higher than 500 m3/day) were obtained as follows; flow rate 2.503 L/min, and 2.337 L/min, HRT 1.059 min, 1.134 min, for Al and Fe electrode, respectively. Consumed mass of Al and Fe were of 3.76 times and 8.90 times respectively, were obtained to removed T-P at optimal conditions with potential 10 V, and 0.03% NaCl as electrolyte.

본 연구에서는 혐기성 소화조에서 발생하는 이산화탄소를 충전탑으로 유입하여 MEA, DEA 및 AMP의 화학적 흡수제의 농도변화에 따른 이산화탄소 제거 효율을 검토하여 혐기성 소화조 내에 적용 가능성을 판단하는데 그 목적이 있다. 본 연구에서 실험에 사용된 충전탑은 유리제 Raschig Ring 6×6 mm를 충전한 직경 50 mm, 충전 높이 1.40 m를 사용하였으며, 액체부하는 20 ℓ/hr, 가스부하는 130 ℓ/hr로 고정하여 CO2의 농도를 10%, 20%, 30%로 주입하였을 때 MEA 10% 및 20%에서와 AMP 10의 CO2 제거율을 관찰하였다. 또한 Packed Tower의 지름은 0.288 m, 충전층의 높이는 1 m이며, 실험시스템은 Air, Air/Water 및 Air-CO2/MEA 흡수제로 하였다. 실험결과에 대한 평가는 계산 프로그램을 통하여 추출하였으며, 분리작용 HTUov, 통과단위수 NTUov, 그리고 정확한 농도계산은 측정을 통하여, 가스 그리고 액체부하를 변화시킴으로써 측정범위를 파악하였다. 실험 결과, MEA의 경우 흡수액 농도, 유입 CO2 농도가 높을수록 빠른 파과시간을 가짐을 알 수 있었고, MEA 10%, DEA 10%, AMP 10% 농도에서의 흡수속도는 MEA, DEA, AMP의 순으로 나타났으며, 흡수부하는 AMP, DEA, MEA의 순으로 나타났다. 그리고 흡수액의 모든 혼합비 및 온도 조건에서 MEA의 첨가량이 높아질수록 CO2의 흡수효율이 감소하는 것으로 나타났다. 이러한 실험결과를 바탕으로 혐기성 소화조에 적용할 CO2 흡수 충전탑 내의 흡수액은 MEA을 적용할 경우 가장 높은 효율을 가지는 것으로 판단되었다.

To evaluate the Natural Period of 5 Story Wooden Pagoda in Korea, vibration test was carried out with the microtremors and synchronized human excitation. The natural period and damping constants were obtained and compared with previous research. From the comparison results, the first natural period of tested 5 Story Wooden Pagoda showed similar value with previous research, and many natural period is occurred.

기존의 테이블탑 시스템 연구에서는 주로 프로젝션 기반의 테이블 표면에 컴퓨터 영상을 디스플레이하고 그 테이블 표면에서 사용자는 멀티 터치(Multi-touch)나 탠저블 물체 (Tangible object)로 인터랙션을 한다. 본 연구에서는 확장 가능한 테이블탑 타일드 디스플레이 시스템에서 적외선 카메라 트래킹과 PDA 모바일 인터페이스를 이용하여 다중 사용자의 인터랙션을 지원하는 FishBowl 게임을 개발하였다. 이 게임은 고화질 테이블탑 가상환경과 PDA 모바일 인터페이스가 함께 연동하여 사용자의 상호작용성과 체감을 향상시키고 상하였다. 본 논문에서는 FishBowl 게임과 시스템 설계 및 구현에 대해서 설명한다. 그리고 사용자 관찰을 통하여 발견된 시스템 유용성과 개선점을 토론하고 결론과 향후 연구 방향에 대해 논한다.

본 연구에서는 고해상도 지원을 목적으로 네트워크로 연결된 다중 디스플레이와 컴퓨터를 활용해서 마스터/슬레이브 구조로 구성된 테이블탑 시스템을 구축하였다. 이 분산 테이블탑 시스템은 소프트웨어의 수정 없이 슬레이브 컴퓨터와 모니터를 추가하여 쉽게 확장할 수 있도록 개발되었다. 그리고 이런 확장형 시스템에서 동작하는 인터랙티브 게임의 개발을 쉽게 할 수 있도록 EBITA(Environment for Building Interactive Table Applications) 프레임워크를 개발하였다. EBITA는 적외선 카메라 트랙킹 시스템을 활용하는 탠저블 인터페이스 모듈과 분산 시스템에서의 그래픽 프로그램의 개발을 용이하게 해주는 기능들로 구성되어 있다. 본 논문에서는 카메라 기반 탠저블 인터페이스와 EBITA 프레임워크에 대해서 설명한다. 그리고 EBITA를 활용해서 개발한 게임을 소개한다.

2006년도 고품질 쌀로 선정된 고품벼, 운광벼, 삼광벼를 기존의 일품벼와 대비하여 의성과 경주의 탑라이스 재배지역에서 2년간 적응시험을 하여 각 품종들의 품질과 미질 특성을 조사한 결과는 다음과 같다. 1. 10a당 수량은 의성, 경주 모두 일품벼가 586 kg, 560 kg으로 가장 많은 수량을 보였으나, 완전미 수량은 삼광벼가 의성과 경주에서 각각 519 kg, 495 kg으로 일품벼보다 더 높은 수량을 보였다. 2. 쌀의 외형상 품위에서 완전립 비율은 삼광벼, 고품벼가 90.7%, 82.5%로 일품벼의 77.5%보다 높았다. 3. 단백질 함량은 삼광벼가 6.2%로 가장 낮았으며, 식미치에서는 삼광벼가 85.9%로 가장 높았다. 4. 쌀가루의 점도 특성에서 최고 점도는 의성의 운광벼가 3180으로 가장 높았으며, 경주의 일품벼가 2255로 가장 낮았다. 5. 밥의 물리적 특성에서 경도는 삼광벼가 평균 3174로 가장 낮았으나, 부착성이 -132로 높게 나왔다.

This study presents the characteristics of nocturnal inversion layer and their effect on the concentration variations of surface air pollutants using tethersonde and automatic weather station (AWS, 2 layer tower) system in Ulsan during 2003. The method for the distinction of inversion intensity was decided based on the sum of nocturnal temperature gradient. As the results, there was a close correlation (correlation coefficient of 0.76) between the maximum inversion height obtained from tethersonde and the sum of nocturnal temperature gradient. The air pollutant concentration was also directly proportional to the inversion intensity. When the inversion intensity was strong in the nighttime, ozone (O3) concentration was lower, while nitrogen dioxide (NO2) concentration was higher. The carbon monoxide (CO) concentration was gradually higher according to the nocturnal inversion intensity, whereas sulfur dioxide (SO2) concentration was relatively constant. In addition, we found that there was no correlation between the inversion intensity and TSP concentration.

This study was focused on the investigation of the characteristics of organics and nitrogen removal with the recycle ratio in anoxic/oxic(A/O) packed bed process that consisted of the anoxic reactor and the aerobic reactor. As increasing the recycle ratio by 0.5, 1.0, 2.0, the COD removal efficiency increased by 94.0%, 98.5%, 98.8% respectively. The aerobic reactor showed the perfect nitrification efficiency by 98.5%, 99.2%, 98.0% respectively. The T-N removal efficiency with the recycle ratio, increased by 56%, 67%, 70% respectively. As increasing the recycle ratio by 0.5, 1.0, 2.0, T-P removal efficiency decreased by 62.1%, 57.4%, 51.3% respectively. The process by releasing the stored phosphorus in the anoxic reactor and uptaking the excess phosphorus in the aerobic reactor, occurred well comparatively when recycle ratio is 0.5. But this process did not occur when the recycle ratio is 1.0 and 2.0. And optimum pH of nitrification was about 6～7 and alkalinity decreased as nitrification rate increased. As increasing the recycle ratio in the anoxic reactor, DO concentration and ORP increased.

Packing tower has been used in the chemical industry and the protection of environment for a long time. In the view of environmental protection, purification of exhaust gas can be performance effective by gas absorption in counter-current packing tower. In this study, characteristics of hydraulic and mass transfer were investigated in D. 0.3m × H. 1.4m packing tower with 50mm plastic Hiflow-ring. This study was carried out "Test systems were experimented in conditions of Air, Air/H2O, NH3-Air/H2O, NH3-Air/H2O- H2SO4, and SO2 -Air/H2O-NaOH under steady state". The extent of test included dry and wetting pressure drop, physical law, separation efficiency, and hold-up as function of gas and liquid load.

In this study a packed tower was selected for the treatment apparatus of NH3 gas produced in industry. Formerly, latticework packing has been used in preventive facility of treatment of NH3 gas. However, recently metallic Ralu-Pack 250YC, structured packing, is usually being used in petrochemical production plant. This study is for the application the packing to the NH3 gas treatment in wet scrubbing process. In Air/water system, hydraulic pressure drop dependent of specific liquid load and gas capacity factor was continuous and parallel from graph. The tower height can be determined by the number of transfer unit and the height of transfer unit influenced on liquid distribution.