无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ

无机盐工业 ›› 2026, Vol. 58 ›› Issue (3): 119-126.doi: 10.19964/j.issn.1006-4990.2025-0066

• 催化材料 • 上一篇    

载体性质对丙烯二聚负载钾催化剂性能的影响

冯嘉浩1,2(), 花吉祥1,2, 张欢1,2, 张胜红1,2, 孙培永1,2, 姚志龙1,2()   

  1. 1.北京石油化工学院新材料与化工学院,北京 102617
    2.恩泽生物质精细化工北京市重点实验室,北京 102617
  • 收稿日期:2025-02-12 出版日期:2026-03-10 发布日期:2025-06-13
  • 通讯作者: 姚志龙(1970— ),男,博士,研究员,研究方向为工业催化;E-mail:yaozl@bipt.edu.cn
  • 作者简介:冯嘉浩(2000— ),男,硕士生,研究方向为工业催化;E-mail:472327321@qq.com
  • 基金资助:
    北京市自然科学基金-昌平创新联合基金项目(L234019);北京市教育委员会科技计划项目(KM 201910017010)

Effect of carrier property on catalytic performance of potassium supported catalysts for propylene dimerization

FENG Jiahao1,2(), HUA Jixiang1,2, ZHANG Huan1,2, ZHANG Shenghong1,2, SUN Peiyong1,2, YAO Zhilong1,2()   

  1. 1.College of New Materials and Chemical Engineering,Beijing Institute of Petrochemical Technology,Beijing 102617,China
    2.Beijing Key Laboratory of Enze Biomass Fine Chemical,Beijing 102617,China
  • Received:2025-02-12 Published:2026-03-10 Online:2025-06-13

摘要:

为考察载体的物理化学性质对丙烯二聚负载钾催化剂表面碱强度和催化剂性能的影响规律,以具有不同孔结构和碱强度的碱金属氧化物和盐为载体,采用熔融法负载金属K制备一系列固体超强碱催化剂。利用N2吸附-脱附、CO2-TPD、Hammett滴定、XRD等方法对载体及催化剂进行表征,并在间歇釜式反应器中考察其催化丙烯二聚的性能。各载体负载钾后表面碱强度显著提高,含有K2O2的催化剂具有催化丙烯二聚的效果,其中K2O2含量最高的K/K2CO3催化性能最好,丙烯转化率和4-甲基-1-戊烯(4MP1)选择性分别达到96.13%和86.02%。结果表明:催化剂表面超强碱中心位点主要由负载金属K与载体相互作用形成的K2O2物种提供;载体表面碱强度越高越有利于在催化剂表面形成超强碱中心;在催化丙烯二聚反应中,催化剂表面K2O2物种含量越高丙烯转化率越高,生成目标产物4MP1的选择性与催化剂表面碱性位点的碱强度分布有关;适宜的碱度Hammett指数为33~35,与载体比表面积和平均孔径大小无关。

关键词: 丙烯二聚, 固体碱催化, 催化剂载体, 4-甲基-1-戊烯

Abstract:

A series of solid superbase catalysts were prepared by using alkali metal oxides or salts with different pore structures and alkali strengths as carriers,and supporting metal K by melting method,to investigate the effect of the physical and chemical properties of carrier on the surface alkali strength and the catalytic performance of potassium supported catalysts for propylene dimerization.The carriers and catalysts were characterized by N2 adsorption desorption,CO2-TPD,Hammett titration,XRD and other methods,and their catalytic performance for propylene dimerization was investigated in a batch reactor.The surface alkali strength of each carrier was significantly increased after loading potassium.The catalysts with K2O2 had catalytic effect on propylene dimerization.The K/K2CO3 catalyst had the highest K2O2 content and showed the best catalytic performance,offered a propylene conversion and 4MP1 selectivity at 96.13% and 86.02%,respectively.It was indicated that the central superbase sites of the catalyst surface were mainly provided by the K2O2 species formed by the interaction between the supported metal K and the carrier.The carriers with higher surface alkali strength were more conducive to the formation of central superbase sites on the catalyst surface.In the catalytic propylene dimerization reaction,the higher the content of K2O2 species on the catalyst surface,the higher the conversion rate of propylene.The selectivity of producing the target product 4MP1 was related to the distribution of alkaline strength of the basic sites on the catalyst surface and the suitable Hammett index range for alkaline strength was 33~35.It was independent of the specific surface area and average pore size of the carriers.

Key words: propylene dimerization, solid base catalyst, catalyst support, 4-methyl-1-pentene

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