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Methyldecalin hVdrocracking over palladium/dzeolite-X

机译:甲基十氢化萘在钯/沸石-X上的氢裂解

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摘要

Hydrocracking of methyldecalin over Pd/REX has been studied with surface sensitive techniques in the critical temperature range 325- 350deg.C. Results from in situ characterization of adsorbed species, and post-reaction analysis of the catalyst surface by infrared and photo- emission spectroscopies, were related to product distributions. The results are discussed in light of quantum chemical calculations of free and catalyst bound intermediates, following ring-opening reactions. Liquid and gaseous products were detected by infrared and UV/Vis spectroscopies. Apparent activation energies of product formation hydrogen consumption, over a broader temperature range, were derived from previous autoclave experiments. An increase in temperature, 325--350deg.C, results in a shift from preferred cracking products to aromatics, an enhanced level of light hydrocarbon off-gases, and a higher coverage of carbonaceous residues. The increased level of carbonaceous residues is accompanied by a lowered coverage of the reactant, at the surface. The altered product distribution can be characterized by apparent single activation energies, valid from 300 to 450deg.C. Methane and aromatics show a similar rapid increase with temperature, hydrogen consumption a more timid increase, indicating a reaction limited by diffusion, and cycloalkane production a modest inverse temperature dependence. Fully hydrogenated ring-opening products represent valuable fuel components, but hydrogen deficiency can instead lead to chemisorbed precursors to coke. Our calculations show that cyclohexane, l,2-diethyl, 3-methyl has a lower heat of formation than the corresponding surface intermediates, but a small enthalpy advantage can easily be countered by entropy effects at higher temperatures. This balance is critical to the formation of preferred products, instead of catalyst deactivation and aromatics. The theoretical results further show that surface intermediates, where the terminating hydrogen is replaced by a C--O bond, have distinct vibrations around l l50 cm~-l.
机译:甲基十氢化萘在Pd / REX上的加氢裂化已通过表面敏感技术在325-350°C的临界温度范围内进行了研究。吸附物质的原位表征结果以及通过红外和光发射光谱法对催化剂表面进行后反应分析的结果与产物分布有关。根据开环反应后游离和催化剂结合的中间体的量子化学计算讨论了结果。通过红外和UV / Vis光谱学检测液体和气体产物。在较宽的温度范围内,产物形成氢消耗的表观活化能来自先前的高压釜实验。温度升高325--350°C,导致从优选的裂化产品转向芳烃,轻烃废气水平提高,碳质残渣覆盖率更高。碳质残留物含量的增加伴随着表面反应物覆盖率的降低。改变的产物分布的特征在于表观的单活化能,其在300至450℃下有效。甲烷和芳烃随温度显示出类似的快速增加,氢消耗更为怯tim地增加,表明反应受到扩散的限制,而环烷烃的产生则与温度成反比。完全氢化的开环产物代表了宝贵的燃料成分,但氢缺乏会导致化学吸附的焦炭前体。我们的计算表明,环己烷,1,2-二乙基,3-甲基具有比相应的表面中间体更低的形成热,但较小的焓值优势可以通过较高温度下的熵效应轻易抵消。这种平衡对形成优选产物至关重要,而不是催化剂失活和芳烃。理论结果进一步表明,表面中间体(其中的末端氢被C-O键取代)在大约150cm-1处具有明显的振动。

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