首页> 外文期刊>Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications >CATALYTIC DEHYDROGENATION OF 10,11-DIHYDRO-5H-DIBENZ[B.F]AZEPINE (IMINODIBENZYL) TO 5H-DIBENZ[B.F]AZEPINE (IMINOSTILBENE) OVER POTASSIUM-PROMOTED IRON OXIDES
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CATALYTIC DEHYDROGENATION OF 10,11-DIHYDRO-5H-DIBENZ[B.F]AZEPINE (IMINODIBENZYL) TO 5H-DIBENZ[B.F]AZEPINE (IMINOSTILBENE) OVER POTASSIUM-PROMOTED IRON OXIDES

机译:钾促进的铁氧化物上的10,11-二氢-5H-二苯并[B.F]阿苯丁胺(亚氨基二苯甲基)催化脱氢成5H-二苯并[B.F]阿苯丁胺(亚氨基二苯乙烯)

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摘要

The catalytic dehydrogenation of 10,11-dihydro-5H-dibenz[b.f]azepine(iminodibenzyl) to 5H-dibenz[b.f]azepine (iminostilbene) has been investigated over potassium-promoted iron oxide catalysts in the presence of steam. The reaction was performed at 550-600-degrees-C and steam/iminodibenzyl ratios of 50-300 mol/mol. Under the conditions used selectiviies to iminostilbene up to 80% at nearly 100% iminodibenzyl conversion were achieved. The observed overall reaction behaviour was influenced by contributions from heterogeneous (catalytic) and homogeneous (non-catalytic) reactions. The homogeneous reaction pathway became prominent at high space time factors (W(cat)/F(IDB) > 2 g(cat) h/g(IDB) and/or high temperatures above 600-degrees-C. Potassium-promoted catalysts (7 wt.-% K) prepared from different iron oxide phases, hematite, maghemite and magnetite, showed all similar selectivities to iminostilbene, indicating that the choice of the iron oxide precursor had no significant influence on the selectivity of the final potassium-promoted iron oxide catalyst. The activity of the catalysts increased with higher BET surface area. The behaviour of all catalysts was strongly influenced by the steam/iminodibenzyl ratio in the feed. Both selectivity to iminostilbene and conversion of iminodibenzyl increased with higher steam/iminodibenzyl ratios. The different roles of steam in the catalytic reaction are discussed. [References: 28]
机译:已经研究了在蒸汽存在下,在钾促进的氧化铁上,将10,11-二氢-5H-二苯并[b.f]氮杂环庚烷(亚氨基二苄基)催化脱氢成5H-二苯并[b.f]氮杂氮烷(亚氨基二苯乙烯)。反应在550-600℃和水蒸气/亚氨基二苄基比为50-300摩尔/摩尔下进行。在所使用的条件下,在接近100%的亚氨基二苄基转化率下,亚甲基二苯乙烯的选择性高达80%。所观察到的总体反应行为受到非均相(催化)反应和均相(非催化)反应的影响。在高时空因子(W(cat)/ F(IDB)> 2 g(cat)h / g(IDB)和/或600摄氏度以上的高温)下,均相反应途径变得突出。由不同的氧化铁相,赤铁矿,磁赤铁矿和磁铁矿制得的7 wt。%K)表现出与亚氨基二苯乙烯相似的所有选择性,表明氧化铁前体的选择对最终钾促进铁的选择性没有显着影响催化剂的活性随BET表面积的增加而增加。所有催化剂的行为均受进料中水蒸气/亚氨基二苄基比的强烈影响。亚氨基二苯乙烯的选择性和亚氨基二苄基的转化率随水蒸气/亚氨基二苄基的比例的增加而增加。讨论了蒸汽在催化反应中的不同作用[参考文献:28]

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