摘要
为了提高烯烃歧化催化剂的性能,以WO 3/SiO 2为研究对象,研究了不同氧化物(MgO、CaO、BaO、SiO 2)对其催化性能的影响。首先比较了各种氧化物对1-丁烯异构反应的作用强弱,之后考察了不同氧化物与WO 3/SiO 2催化剂混合装填对1-丁烯自歧化反应的影响。结果表明:不同氧化物的异构活性由大到小的顺序为CaO、BaO、MgO、SiO 2;掺混MgO与SiO 2可以使反应体系稳定性更强;而与SiO 2相比,MgO更好地促进了交叉歧化反应,使丙烯的选择性提高。最后研究了MgO掺混量对乙烯和顺-2-丁烯歧化制丙烯反应的影响,发现MgO的最佳掺混质量分数为30%。
Currently,WO 3/SiO 2 catalyst is the only industrialized olefin metathesis catalyst due to its low cost and strong anti-toxicity,but it needs to mix with promoters to maintain the high activity and stability.In order to improve this process,the effects of different oxides(MgO,CaO,BaO,SiO 2)on the catalytic performance of WO 3/SiO 2 catalyst were investigated.The effects of oxides on 1-butene isomerization were tested firstly,with a descending order of CaO,BaO,MgO,SiO 2.The self-metathesis of 1-butene was then studied under the catalysis of WO 3/SiO 2 mixed with different oxides,in which MgO and SiO 2 can make the reaction more stable.While the propylene selectivity in the MgO system was higher than that in SiO 2 system,due to the accelerated cross-metathesis between 1-butene and 2-butene,which generates from the isomerization of 1-butene over MgO.Finally,the effects of different loading mass fraction of MgO in the metathesis of ethylene and cis-2-butene was studied.Results show that the optimum loading mass fraction of MgO is 30%.
作者
姜伟丽
籍星
郭崴
冯硕
黎正熙
孙曼颖
陈雅琪
周广林
周红军
JIANG Weili;JI Xing;GUO Wei;FENG Shuo;LI Zhengxi;SUN Manying;CHEN Yaqi;ZHOU Guanglin;ZHOU Hongjun(State Key Laboratory of Heavy Oil Processing,College of New Energy and Materials,China University of Petroleum,Beijing 102249,China;Tsinghua University High School-Aosen,Beijing 100016,China)
出处
《石油学报(石油加工)》
EI
CAS
CSCD
北大核心
2021年第3期611-618,共8页
Acta Petrolei Sinica(Petroleum Processing Section)
基金
国家自然科学基金青年基金资助项目(21306227)资助。
关键词
催化
多相反应
歧化
烯烃
氧化钨
氧化物
catalysis
heterogeneous reaction
metathesis
olefin
tungsten oxide
oxide