Influence of gold promoter on Fischer Tropsch synthesis Over Co/Al2O3 catalysts

N. Ahmad, S. Hussain, B. Muhammad, J. A. Anderson, N. Ali, S. Abbas
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引用次数: 4

Abstract

In order to enhance the catalytic activity of Alumina supported cobalt catalyst (Co/Al2O3) for Fischer Tropsch synthesis, 1.5 and 2.5 wt% Au promoted 10% Co/Al2O3 is synthesized by coprecipitation and impregnation methods. The synthesized catalysts are characterized using XRD, TPR, TGA and BET techniques while fixed bed micro reactor is used to evaluate the activity and selectivity of prepared catalysts. The results confirm that 1.5 wt% Au loading shows higher CO conversion and C5+ hydrocarbons selectivity along with decreased selectivity towards methane and lower hydrocarbons. It is proposed through TPR studies that Au addition enhances the reduction of cobalt oxide thereby increasing the number of active sites and hence catalytic efficiency. Additionally, an increase in pressure and reduced feed flow rate led to excessive hydrocarbons production and subsequent conversion of syngas, possibly due to extended contact time between catalyst and reactants.
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金助剂对Co/Al2O3催化剂Fischer - Tropsch合成的影响
为了提高氧化铝负载钴催化剂(Co/Al2O3)在Fischer - Tropsch合成中的催化活性,采用共沉淀法和浸渍法合成了1.5 wt% Au和2.5 wt% Au促进的10% Co/Al2O3。采用XRD、TPR、TGA和BET等技术对合成的催化剂进行了表征,并利用固定床微反应器对催化剂的活性和选择性进行了评价。结果证实,1.5 wt%的Au负载具有较高的CO转化率和C5+碳氢化合物选择性,但对甲烷和低碳氢化合物的选择性降低。通过TPR研究提出,Au的加入增强了氧化钴的还原,从而增加了活性位点的数量,从而提高了催化效率。此外,压力的增加和进料流量的降低可能会导致过量的碳氢化合物产生和随后的合成气转化,这可能是由于催化剂和反应物之间接触时间的延长。
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