Highly selective conversion of methanol to propylene: design of an MFI zeolite with selective blockage of (010) surfaces

被引:19
作者
Cai, Dali [1 ]
Wang, Ning [1 ,2 ]
Chen, Xiao [1 ]
Ma, Yunhai [1 ,3 ]
Hou, Yilin [1 ]
Li, Xinghua [2 ,4 ]
Zhang, Chenxi [1 ]
Chen, Zhaohui [1 ]
Song, Wenlong [1 ]
Arslan, Muhammad Tahir [1 ]
Li, Yiru [1 ,5 ]
Wang, Yao [1 ]
Qian, Weizhong [1 ]
Wei, Fei [1 ]
机构
[1] Tsinghua Univ, Beijing Key Lab Green React Engn & Technol, Dept Chem Engn, Beijing, Peoples R China
[2] King Abdullah Univ Sci & Technol, Adv Membranes & Porous Mat Ctr, Phys Sci & Engn Div, Thuwal, Saudi Arabia
[3] SINOPEC Res Inst Petr Proc, Beijing, Peoples R China
[4] Northwest Univ, Sch Phys, Xian, Shaanxi, Peoples R China
[5] Purdue Univ, Davidson Sch Chem Engn, W Lafayette, IN 47907 USA
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
PARA-XYLENE SELECTIVITY; SHAPE SELECTIVITY; OLEFINS; AROMATICS; ZSM-5;
D O I
10.1039/c8nr10371b
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
As an important catalyst of methanol-to-propylene (MTP) conversion, the ZSM-5 zeolite has an anisotropic diffusion path and a large pore size, resulting in the formation of undesirable heavy aromatic by-products. Herein, we developed a surface-specific silica deposition method to block straight channels of nanosized ZSM-5 crystals selectively. By such a coating method, we can selectively suppress the yield of aromatics from the original 13% to 2.4% at 100% conversion of methanol. Trapped hydrocarbon pool species are directly confirmed by aberration-corrected S/TEM for the first time. Such a method of trapping and restricting hydrocarbon pool species in a multiscale zeolite with 10-membered rings would significantly increase its catalytic efficiency and olefin diffusion. Moreover, this provides new methodologies for zeolite structure construction and will be greatly beneficial for the industrial MTP process.
引用
收藏
页码:8096 / 8101
页数:6
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