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Catalytic Co_2/H_2 Methanation Reaction Over Alumina Supported Manganese/Cerium Oxide Based Catalysts

机译:催化CO_2 / H_2甲烷化反应在氧化铝中负载的锰/氧化铈基催化剂

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The methanation reaction is a promising method for the purification of natural gas, in which the acid gas of CO_2, is eliminated by catalytic conversion. The advantage of catalytic technology is the utilization of CO_2 present for the production of methane gas. The used of alumina supported cerium oxide as the based catalyst in CO_2/H_2 methanation reaction have been investigated in this research by using manganese as the dopant and ruthenium as the co-dopant via wet impregnation technique. The series of cerium oxide catalysts calcined at 400°C for 5 hours had been prepared at the screening stage. Then, the catalysts were optimized by different calcination temperatures and different based oxide loadings. The potential catalysts of Ru/Mn/Ce (5:35:60)/Al_2O_3 calcined at 700°C gave 100% of CO_2 conversion by using Fourier Transform Infrared (FTIR) spectroscopy and yielded about 80% of CH_4 at reaction temperature of 400°C. X-ray Diffraction (XRD) analysis showed that the supported catalysts were amorphous in structure. Field Emission Scanning Electron Microscopy (FESEM) analysis illustrated the surface of the catalysts were covered with small and dispersed spherical particles. Energy Dispersion X-ray (EDX) analysis revealed that there was 1.02% reduction of Ru in the Ru/Mn/Ce (5:35:60)/Al_2O_3 used catalysts compared to fresh catalysts. Meanwhile Nitrogen Adsorption (NA) analysis showed that Ru/Mn/Ce (5:35:60)/Al_2O_3 catalyst attained surface area of 143.10 m~2/g at 700°C.
机译:甲烷化反应是天然气的纯化,其中CO_2的酸性气体,是由催化转化消除了有前途的方法。催化技术的优点是本CO_2用于生产甲烷气体的利用率。氧化铝支撑的铈氧化物作为在CO_2 / H_2甲烷化反应基于催化剂的使用已经在本研究通过使用锰作为掺杂剂和钌作为通过湿浸渍技术的共掺杂剂的影响。已在筛选阶段中制备的系列在400℃下煅烧5小时的氧化铈催化剂。然后,将催化剂通过不同煅烧温度和不同的基于氧化物的负载优化。钌/锰/ Ce的潜在催化剂(5:35:60)/ Al_2O_3的煅烧在700℃下得到CO_2转换的100%通过使用傅里叶变换红外光谱(FTIR)和在400反应温度产生约CH_4的80% ℃。 X-射线衍射(XRD)分析结果表明,负载型催化剂在结构上无定形的。场发射扫描电子显微镜(FESEM)分析示出的催化剂的表面覆盖着小并且分散的球形颗粒。能量色散X射线(EDX)分析表明,有钌的钌/锰/ CE(5:35:60)1.02%的减少/ Al_2O_3的使用的催化剂相比,新鲜的催化剂。同时氮吸附(NA)分析表明,钌/锰/ CE(5:35:60)/ Al2O3催化剂达到表面的143.10米〜2 / g的在700℃的区域。

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