The pure Ti, Ni and carbon powders were reaction milled to synthesize the TiC-Ni based cermet powders with ultrafine microstructures. After milling, the ultrafine TiC or amorphous Ti-Ni phase was obtained, respectively, according to the milling condition. The effects of milling variables on the synthesizing behavior of the powders were investigated in detail. The sintered TiC-Ni based cermet of the reaction milled powders consisted of very fine TiC of 0.2~1.5m, as compared with that of a commercial cermet of 3~5m. This demonstrates the potenial of reaction milling as an effective processing route for the preparation of cermet materials.

The Cuo-Magnetite and ZnO-Magnetite catalysts with various of Cuo and ZnO mole% for Carbon Dioxide decomposed reaction synthesized. The catalysts were reduced by H2 at 350℃ for 3 hours. The temperature was obtained by TGA and DSC experiments. The structures of catalysts were confirmed by X-ray diffraction experiment. The surface area of catalysts is 15~27 m2/g. The results of Carbon Dioxide decomposed ability was better H2-reduced magnetite catalysts with 0.03 mole% CuO and 0.03 mole% ZnO than others catalysts. After Carbon Dioxide decomposed reaction, catalysts were reacted H2 and created only methane.

본 연구에서는 고령토, 유황, 탄산나트륨, 규석 및 송진을 원료로 하여 군청을 합성하였고, 그 반응 메카니즘을 조사하였다. 원료의 혼합시료는 군청의 중간 생성물인 녹색군청을 합성하기 위하여, 820˚C에서 4시간 동안 소성하였다(승온율 2˚C/min). 합성된 녹색군청은 최종적으로 군청을 얻기 위해 500˚C에서 산화처리하였다. 합성 과정에서 발생하는 반응 생성물 및 이들의 구조적 변화는 x선 회절 분석과 Raman Spectrum 분석에 의하여 평가하였다. 소성과정에서 황화나트륨은 500˚C에서 생성되었고, NaAISiO4는 620˚C에서 형성되었다. 그리고, 녹색군청은 황화나트륨과 NaAISiO4의 반응에 의하여 740˚C부근에서 형성하기 시작하였다. 또한, 청색군청의 형성은 녹색군청 중에 잔존하던 황화타트륨의 산화로 방출되는 유황 원자에 기인하였다.

본 연구에서는 폐자원 합성가스를 이용한 고온전이반응용 Ce가 첨가된 Cu/γ-Al2O3 촉매의 물리 화학적 특성을 비교 분석하였다. 합성방법에 따른 촉매의 특성을 비교하기 위해 활성물질의 담지 순서를 변경하여 Ce/Cu/γ-Al2O3, Ce-Cu/γ-Al2O3, Cu/Ce/γ-Al2O3, Cu/γ-Al2O3 촉매를 제조하였다. 제조된 촉매 중 Ce/Cu/γ-Al2O3 촉매가 가장 높은 활성도 및 안전성을 나타냈다. 제조된 촉매의 물리-화학적 특성은 XRD, H2-TPR, XPS, Raman, Photoluminescence 등으로 분석하였다. 그리고 CO 전환율에서도 CeO2로 첨가된 모든 Cu/γ-Al2O3 촉매는 Cu/γ-Al2O3보다 높은 CO 전환율을 보였다. 이 연구결과는 CeO2의 첨가가 고온전이반응에서 Cu/γ-Al2O3 촉매의 성능을 향상 시킨 것을 나타낸다. 또한, Ce/Cu/γ-Al2O3 촉매의 높은 촉매 활성은 주로 고농도 산소저장능 및 환원된 Cu종과 관련이 있음을 알 수 있었다.

Magnetite (Fe3O4) has been prepared directly to avoid the reduction process prior to the H2 production from the high temperature water gas shift reaction of the simulated waste derived synthesis gas. Citric acid has been employed as a complexing agent for the direct synthesis of magnetite. Notably, without the reduction process, the catalyst prepared at the citric acid molar ratio of 1.0 showed 80% CO conversion at 350℃ at a gas hourly space velocity of 40,057 h-1.

Simulated waste-derived synthesis gas has been tested for hydrogen production through water gas shift (WGS) reaction in the temperature range of 240oC ~ 400oC over supported Pt catalysts prepared by an incipient wetness impregnation method. MG30, MgO, ZrO2, Al2O3 and CeO2 were employed as supports for WGS reaction in this study. 1 wt.% Pt/ CeO2 catalyst exhibited the highest CO conversion as well as 100% CO2 selectivity. This is due to easier reducibility of Pt/CeO2 and high oxygen mobility and oxygen storage capacitiy of CeO2. Pt/CeO2 catalyst can be a promising catalyst for WGS reaction from waste-derived synthesis gas.