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Titanium and copper oxide based catalysts for the in-situ reactions of methanation and desulfurization in the removal of sour gases from simulated natural gas

机译:钛和铜氧化物基催化剂,用于甲烷化和脱硫的原位反应,用于从模拟天然气中去除酸性气体

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摘要

The objective of this novel catalyst development is to achieve both low temperature and high conversion of sour gases. Supported mixed metal oxide catalysts were prepared by impregnating the catalysts on alumina beads for the in-situ reactions of H2S desulfurization and CO2 methanation from room temperature up to 200oC. The results showed that the 100% conversion of H2S to elemental sulfur for all of the potential catalysts was achieved at 100oC. However, methanation of CO2 in the presence of H2S yielded 0.4% CH4 over Fe/ Zn/ Cu/ Ti-Al2O3 catalyst and 0.7% CH4 over Fe/ Zn/ Cu-Al2O3 catalyst at maximum studied temperature of 200oC. XPS results indicated that spinel compounds of CuFe2O4 and Fe3O4 act as the active sites on the Fe/ Zn/ Cu-Al2O3 and Fe/ Zn/ Cu/ Ti-Al2O3 catalysts. The appearance of Fe3+-OH on Fe/ Zn/ Cu/ Ti-Al2O3 catalyst increased its H2S desulfurization activity. N2 adsorption-desorption analysis illustrated that 34% of the surface area of Fe/ Zn/ Cu-Al2O3 catalyst was reduced while Fe/ Zn/ Cu/ Ti-Al2O3 catalyst showed reduction of 17% after catalytic testing, which indicated the deactivation of the catalysts resulted from sulfur poisoning
机译:这种新型催化剂开发的目的是实现低温和酸性气体的高转化率。负载型混合金属氧化物催化剂的制备方法是,将催化剂浸渍在氧化铝珠上,以进行H2S脱硫和CO2甲烷化的原位反应(室温至200oC)。结果表明,对于所有潜在的催化剂,H2S均能在100°C下100%转化为元素硫。然而,在最高研究温度为200oC的条件下,在H2S存在下进行CO2甲烷化可得到比Fe / Zn / Cu / Ti-Al2O3催化剂高0.4%的CH4和比Fe / Zn / Cu-Al2O3催化剂高0.7%的CH4。 XPS结果表明,CuFe2O4和Fe3O4的尖晶石化合物在Fe / Zn / Cu-Al2O3和Fe / Zn / Cu / Ti-Al2O3催化剂上具有活性。 Fe / Zn / Cu / Ti-Al2O3催化剂上Fe3 + -OH的出现增加了H2S的脱硫活性。 N 2吸附-解吸分析表明,催化测试后,Fe / Zn / Cu-Al2O3催化剂的表面积减少了34%,而Fe / Zn / Cu / Ti-Al2O3催化剂的表面积减少了17%,表明该催化剂的失活。硫中毒导致的催化剂

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