石油炼制与化工 ›› 2026, Vol. 58 ›› Issue (7): 64-72.

• 基础研究 • 上一篇    下一篇

Al2O3载体低P改性对1-丁烯临氢异构化性能的影响

岳金月,张鹏程,巩笑笑,董明会   

  1. 中石化石油化工科学研究院有限公司 石油化工分子转化与反应工程全国重点实验室
  • 收稿日期:2026-02-03 修回日期:2026-03-05 出版日期:2026-07-12 发布日期:2026-06-29
  • 通讯作者: 董明会 E-mail:dongminghui.ripp@sinopec.com
  • 基金资助:
    非碱水洗干式分离技术与装备

EFFECT OF LOW-PHOSPHORUS MODIFICATION OF Al2O3 SUPPORT ON THE PERFORMANCE OF 1-BUTENE HYDROISOMERIZATION

  • Received:2026-02-03 Revised:2026-03-05 Online:2026-07-12 Published:2026-06-29

摘要: 针对混合碳四馏分资源化利用中1-丁烯异构化的需求,采用等体积浸渍法制备了一系列P改性的Pd-P/Al2O3催化剂,考察了其在1,3-丁二烯选择性加氢协同1-丁烯异构化反应中的性能。通过一系列表征手段,研究了P负载量对催化剂表面酸性、金属分散性及电子结构的影响。结果表明,P的引入通过形成Al—O—P结构显著调控了催化剂表面的酸性分布,增加了弱L酸中心的密度。尽管P的引入导致Pd颗粒尺寸略有增大,但P与Pd之间的电子相互作用提升了活性组分的电子密度。在温度60 ℃、压力1.8 MPa、质量空速3.5 h-1的条件下,P负载量(w)为0.5%的催化剂表现出最优性能,1,3-丁二烯实现完全转化,1-丁烯异构化率为81.50%,2-丁烯/1-丁烯摩尔比达到14.25,趋近热力学平衡极限。本研究揭示了催化剂表面弱L酸中心与1-丁烯异构化性能之间的构效关系,为工业高效催化剂的开发提供了理论依据。

关键词: 1,3-丁二烯, 选择性加氢, 1-丁烯, 异构化, P改性, 构效关系

Abstract: To meet the requirements of 1-butene isomerization in the resource utilization of mixed C4 fractions, a series of phosphorus(P)-modified Pd-P/Al2O3 catalysts were prepared by the incipient wetness impregnation method. The catalytic performance was investigated in the selective hydrogenation of 1,3-butadiene coupled with 1-butene isomerization. The effects of P loading on the surface acidity, metal dispersion, and electronic structure of the catalysts were studied using a series of characterization techniques. The results indicated that the introduction of P significantly regulated the surface acidity distribution by forming Al—O—P structures, thereby increasing the density of weak Lewis acid sites. Although P loading led to a slight increase in Pd particle size, the electronic interaction between P and Pd enhanced the electron density of the active species. Under the reaction conditions of 60℃, 1.8MPa, and a space velocity of 3.5h-1, the catalyst with a P loading of 0.5% exhibited the optimal performance: 1,3-butadiene was fully converted, the 1-butene isomerization rate reached 81.50%, and the 2-butene/1-butene molar ratio was 14.25, which approached the thermodynamic equilibrium limit. This study reveals the structure-activity relationship between surface weak Lewis acid sites and 1-butene isomerization performance, providing a theoretical basis for the development of highly efficient industrial catalysts.

Key words: 1,3-butadiene, selective hydrogenation, 1-butene, isomerization, phosphorus modification, structure-activity relationship