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        검색결과 5

        1.
        2018.09 KCI 등재 구독 인증기관 무료, 개인회원 유료
        주파수 변화에 따른 에폭시 복합체의 전기적 특성을 알아보기 위하여 온도 범위 20[℃], 100[℃], 140[℃], 주파수 범위 30[Hz]~3[MHz] 사이에서 유전율 및 유전손실을 측정하였다. 저주파 영역에서 유전분산과 유전 손실이 나타나고 있음을 확인하였다. 또한 고온 영역에서는 충진제의 영향으로 유전율이 감소하는 것을 확인하였다.
        4,000원
        2.
        2017.03 KCI 등재 구독 인증기관 무료, 개인회원 유료
        주파수 (30 ~ 300k Hz)와 온도 범위 (20 ~ 160 ℃)가 경화 조건에 따른 에폭시 수지의 전 기적 특성 (유전율 및 유전손실)에 미치는 영향을 조사하였다. 유리전이온도(Tg) 이하에서는 주파수와 상관없이 각각 3가지의 시편에서 유전분산 현상이 나타나지 않으며, 유리전이온도(Tg) 이상에서 유전분 산 현상이 나타났다.
        4,000원
        3.
        2003.06 KCI 등재 구독 인증기관 무료, 개인회원 유료
        Electron transfer through an Langmuir-Blodgett(LB) monolayer film sandwiched between metal electrodes. We used an eicosanoic acid material and the material was very famous as a thin film insulating material. Eicosanoic acid monolayer was deposited by Langmuir-Blodgett(LB) technique and a subphase was a CdCl2 solution as a 2×10-4 mol/L. Also we used a bottom electrode as an Al/Al2O3 and a top electrode as a Al and Ti/Al. Here, the Al2O3 on the bottom electrode was deposited by thermal evaporation method. The Al2O3 layer was acted on a tunneling barrier and insulating layer in tunnel diode. It was found that the proper transfer surface pressure for film deposition was 25 mN/m and the limiting area per molecule was about 24 a2/molecule. When the positive and negative bias applied to the molecular device, the behavior shows that a tunnel switching characteristics. This result were analyzed regarding various mechanisms.
        4,000원
        4.
        1993.01 KCI 등재 구독 인증기관 무료, 개인회원 유료
        Anaerobic Digestion of thickened septage was investigated in this study. Thickening could reduce the volume of septage to be treated to about 40% with 12hr HRT. The VS and BOD removal efficiencies were respectively 28 to 45%, and 75% when digested the thickened septage with 30 day HRT Or $1.4kgVS/m^3/d$. The BOD removal efficiency could be increased to about 90% with subsequent settling tank with about 6 hours HRT. The gas production rate was 0.22 to $0.35m^3gas/kgVSadd$($0.75m^3gas/kgVSrm$), or $1.32m^3gas/kgBOD_{rm}$. In addition, the supernatant of thickener could be returned to the aeration tank treating domestic sewage. In this case, a BOD loading rate of 0.5 to $0.7kgBOD/m^3/d$ or 0.5kgBOD/kgMLVSS/d was proposed for 80% BOD reduction.
        4,000원