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The influence of support on the performance of molybdenum sulfide catalysts used to hydrotreat coal liquids.

机译:载体对用于加氢处理煤液的硫化钼催化剂性能的影响。

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The research described herein involves the development of catalysts for use in hydrotreating coal liquids. A variety of supports for molybdenum sulfide hydrotreating catalysts were studied. These materials included silica, silica-magnesia, titania, chromia-alumina, activated carbon and nitrided activated carbon. The alumina supported, commercial catalysts Amocat 1A and Amocat 1C as well as the silica-alumina supported, commercial catalyst Harshaw CoMo-0402 were also studied.; Catalysts were characterized by BET surface area, mercury porosimetry and x-ray powder diffraction. Acidity was measured by the temperature programmed desorption of tert-butyl amine. Initial activity screening studies were conducted in a stirred autoclave batch reactor to determine appropriate metals loadings for the various supports. Initially active catalysts were then tested in a bench scale, trickle bed reactor to determine activity maintenance, coking tendency and selectivity at lined out conditions. Selectivities for hydrodenitrogenation and for the production of hydrogen donor molecules were of interest. The donatable hydrogen content of the product was determined by {dollar}sp1{dollar}H and {dollar}sp{lcub}13{rcub}{dollar}C NMR spectroscopy.; The results indicated a strong correlation between lined out hydrogenation activity and the volume in 60-200 A diameter pores. It is thought that pores of this size can accommodate the equilibrium coke content without blockage of the active sites. A second correlation was observed between HDN activity and acid site density, indicating the importance of acid sites in denitrogenation. Low acidity catalysts appeared to produce a greater hydrogen donor content in the product oil than did high acidity catalysts but the results were not conclusive. The results also suggest that Bronsted acid sites can markedly reduce coking tendency but that in general, coke formation is related in a complex way to the acid/base chemistry of the surface.
机译:本文所述的研究涉及开发用于加氢处理煤液的催化剂。研究了用于硫化钼加氢处理催化剂的各种载体。这些材料包括二氧化硅,二氧化硅-氧化镁,二氧化钛,氧化铬-氧化铝,活性炭和氮化活性炭。还研究了氧化铝负载的商业催化剂Amocat 1A和Amocat 1C以及二氧化硅-氧化铝负载的商业催化剂Harshaw CoMo-0402。通过BET表面积,汞孔隙率法和X射线粉末衍射对催化剂进行表征。酸度通过叔丁胺的程序升温脱附来测量。在搅拌的高压釜间歇反应器中进行初始活性筛选研究,以确定各种载体的合适金属负载量。然后首先在台式规模的滴流床反应器中对活性催化剂进行测试,以确定在列明条件下的活性维持,焦化趋势和选择性。加氢脱氮和氢供体分子的生产的选择性是令人关注的。产物的可贡献氢含量通过{dol} sp1 {dollar} H和{dollar} sp {lcub} 13 {rcub} {dollar} C NMR光谱法测定。结果表明,衬里的氢化活性与直径为60-200 A的孔中的体积之间具有很强的相关性。据认为,这种尺寸的孔可以容纳平衡的焦炭含量而不会阻塞活性部位。观察到HDN活性与酸性位点密度之间存在第二种相关性,表明酸性位点在脱氮中的重要性。低酸度催化剂似乎比高酸度催化剂在产物油中产生更高的氢供体含量,但结果尚无定论。结果还表明,布朗斯台德酸位点可以显着降低焦化趋势,但总的来说,焦炭的形成与表面的酸/碱化学性质具有复杂的关系。

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