摘要
催化重整是原油二次加工结构调整和产品升级的核心技术之一。工业上Pt催化剂面临着主要由氢解引起的选择性不高的问题,高分散的Pt中心有利于抑制氢解副反应[1],提高异构、环化选择性[1]。本工作利用水滑石层板上原子级均匀分布的Sn(IV)诱导负载制备了高分散Pt催化剂(图1a),Pt分散度为96%,单原子和小于10个Pt原子组成的原子簇占91%。相比之下,Pt Sn直接负载在Mg Al-LDH/Al_2O_3和Al_2O_3上制得的催化剂,分散度分别为85%和80%,单原子和小Pt簇比例分别为62%和41%。在正庚烷重整反应中,高分散的Pt催化剂有效地抑制了氢解并明显提高了代表环化能力的C7产物选择性(图1b和图1c)。
Conventional supported Pt for industrially catalytic reforming suffers low selectivity due to hydrogenolysis reaction.The development of highly dispersed Pt offers the opportunities for settling this problem [1].Herein,a supported Pt,with Pt dispersed in single atoms plus small clusters with fewer than 10 atoms(91%) on Sn-containing mixed metal oxides,was prepared by the inducement of Sn component confined in the lattices of brucite-like layers of layered double hydroxides(LDHs)(Fig.1a).The highly dispersed Pt effectively inhibited the hydrogenolysis and significantly improved the selectivity to cyclization products in the n-heptane reforming reaction(Fig.1b and c).
引文
[1]Flaherty,D.W.;Iglesia,E.J.Am.Chem.Soc.2013,135:18586.