Abstract
Carbon dioxide hydrogenation reaction was carried out over hybrid catalyst composed of $Cu/ZnO/ZrO_2$, and MFI zeolites such as HZSM-5, H-Ga-Silicate and H-Fe-Silicate. The hybrid catalyst composed of $Cu/ZnO/ZrO_2$, catalyst and HZSM-5 showed the highest yield and selectivity to $C_2{^+}$ hydrocarbon, which seemed to be due to the largest amount of Br nsted acid sites. Higher yield to $C_2{^+}$ hydrocarbon was obtained over HZSM-5 with lower $SiO_2/Al_2O_3$ ratio and also with longer ion exchange time, which showed larger amount of Br nsted acid sites, respectively. When a metal ion was exchanged into HZSM-5, the highest yield to $C_2{^+}$ hydrocarbon was obtained with descending order $Ga/HZSM-5{\simeq}HZSM-5>Zn/HZSM-5$, i.e., with the amount of $Br\ddot{o}nsted$ acid sites.
$Cu/ZnO/ZrO_2$와 MFI계열의 제올라이트(HZSM-5, H-Ga-Sllicate, H-Fe-Silicate)로 이루어진 혼성촉매상에서 이산화탄소 접촉수소화반응을 수행하였다. MFI계열의 제올라이트중 브뢴스테드 산점양이 가장 많은 HZSM-5를 포함한 혼성촉매가 가장 높은 $C_2{^+}$ 탄화수소 수율을 나타내었다. HZSM-5를 포함한 혼성촉매 중에서는 $SiO_2/Al_2O_3$비가 낮을수록, 이온교환 시간이 많을수록 즉 브뢴스테드 산점의 양이 많을수록 $C_2{^+}$ 탄화수소에 대한 수율이 높았다. HZSM-5에 금속이온을 이온 교환 하였을 경우, $HZSM-5{\simeq}Ga/HZSM-5>Zn/HZSN-5$의 순서로 활성이 높았는데 이 또한 브뢴스테드 산점수가 많을수록 활성이 증가하였다.
