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Metal-ion pillared clays as hydrocracking catalysts (II): effect of contact time on products from coal extracts and petroleum distillation residues

机译:金属离子柱状粘土作为加氢裂化催化剂(II):接触时间对煤提取物和石油蒸馏残渣产物的影响

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Novel catalysts have been prepared, based on montmorillonite (a natural clay) and laponite (a synthetic clay) pillared with tin, chromium and aluminium pillars as well as layered double hydroxides based on polyoxo-vanadate and -molybdate as previously described. These novel catalysts were compared initially with a standard Ni/Mo catalyst supported on alumina and a dispersed catalyst, Mo(CO)_6 in hydrocracking a coal extract for a short contact time of 10 mm at 440 deg C in a microbomb reactor with tetralin solvent and hydrogen at a pressure of 190 bar. In the present work, the best of the novel catalysts, chromium montmorillonite calcined at 500 deg C and tin laponite, have been compared with the supported catalyst and a dispersed catalyst (Mo(CO)_6) in the repeated hydrocracking of fresh coal extract over three sequential periods of 1 h. Also, the chromium montmorillonite calcined at 500 deg C has been used in the hydrocracking of primary coal extracts, prepared in the flowing solvent liquefaction rig from Pittsburgh #8 and Illinois #6 coals, for reaction times of 10 mm and 2 h. Further, the chromium montmorillonite calcined at 500 deg C and tin laponite, have been compared with the supported catalyst and in the absence of a catalyst, in the hydrocracking of a petroleum distillation residue with 10 mm and 2 h reaction times. Results were compared by size exclusion chromatography in NMP solvent and by UV-fluorescence and evaluated by the extent of the shift of the SEC profile to small molecules and by the shift of the synchronous UV-fluorescence profiles to shorter wavelengths. The performances of both catalysts at short, long or repeated reaction times are seen to be better than that of the conventional NiMo catalyst for the hydrocracking of coal-derived materials and a petroleum residue. Trials on a longer time scale are necessary in the next level of evaluation.
机译:如前所述,基于以锡,铬和铝为支柱的蒙脱土(天然粘土)和锂皂石(合成粘土)以及基于聚氧钒酸盐和钼酸盐的层状双氢氧化物制备了新型催化剂。首先将这些新型催化剂与负载在氧化铝上的标准Ni / Mo催化剂和分散催化剂Mo(CO)_6在含四氢化萘溶剂的微型炸弹反应器中于440℃下加氢裂化煤提取物10毫米的短接触时间进行了比较。和氢气,压力为190 bar。在目前的工作中,最好的新型催化剂,即在500℃煅烧的铬蒙脱土和锡皂石与负载型催化剂和分散催化剂(Mo(CO)_6)在新鲜煤提取物的反复加氢裂化过程中进行了比较。三个连续的1小时周期。同样,在500摄氏度下煅烧的铬蒙脱石已用于一次煤提取物的加氢裂化,该反应是在流动的溶剂液化装置中从匹兹堡8号和伊利诺伊州6号煤制备的,反应时间为10毫米和2小时。此外,在石油蒸馏残渣的加氢裂化中,在10毫米和2小时的反应时间下,将在500℃煅烧的铬蒙脱石和锂皂石与负载型催化剂进行了比较。通过在NMP溶剂中的尺寸排阻色谱法和通过UV荧光比较结果,并通过SEC轮廓向小分子的移动程度和同步UV荧光向较短波长的移动来评估结果。可见,两种催化剂在短,长或重复反应时间上的性能均优于传统的NiMo催化剂,用于煤衍生材料和石油残渣的加氢裂化。在下一级评估中,必须进行较长时间的试用。

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