Two-stage glucose-assisted crystallization of ZSM-5 to improve methanol to propylene (MTP)

被引:42
作者
Feng, Rui [1 ]
Wang, Xixi [1 ]
Lin, Jiawei [1 ]
Li, Zheng [1 ]
Hou, Kun [1 ]
Yan, Xinlong [1 ]
Hu, Xiaoyan [1 ]
Yan, Zifeng [2 ]
Rood, Mark J. [3 ]
机构
[1] China Univ Min & Technol, Sch Chem Engn & Technol, Minist Educ, Key Lab Coal Proc & Efficient Utilizat, Xuzhou 221116, Jiangsu, Peoples R China
[2] China Univ Petr, State Key Lab Heavy Oil Proc, Key Lab Catalysis, Qingdao 266580, Peoples R China
[3] Univ Illinois, Dept Civil & Environm Engn, 205N,Mathews Ave, Urbana, IL 61801 USA
关键词
ZSM-5; Two-stage crystallization; Glucose; Acid sites; Methanol to propylene; TO-HYDROCARBONS CONVERSION; MODIFIED HZSM-5 ZEOLITES; CORE-SHELL CATALYSTS; HIGH-SILICA HZSM-5; OLEFINS PROCESS; MFI ZEOLITE; ACID SITES; H-ZSM-5; DEACTIVATION; SELECTIVITY;
D O I
10.1016/j.micromeso.2018.05.003
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Improving propylene selectivity and the lifetime of ZSM-5 catalyst is of great significance for methanol to propylene (MTP) reaction. Hierarchical ZSM-5 zeolites were synthesized by a two-stage crystallization method using glucose as a second template. The structural and surface properties and the morphologies of the prepared samples were characterized by low-temperature N-2 sorption, XRD, Al-27 and Si-29 NMR, FTIR using pyridine probe molecule, NH3-TPD, SEM, and TEM analysis. The two-stage glucose-assisted crystallized ZSM-5 zeolites exhibited large prismatic crystallites, increased intracrystalline mesopores, and reduced acid amount and acid strength, compared with the conventional one-stage crystallized ZSM-5. Methanol to propylene (MTP) reaction at 450 degrees C and methanol WHSV of 3.8 h(-1) revealed that the newly prepared ZSM-5 catalyst, such as ZSM-5-T3, exhibited highest propylene selectivity of 45.2%, propylene to ethylene ratio of 8.4, and C-2(-)center dot C-4(-) selectivity of 63.9%.
引用
收藏
页码:57 / 66
页数:10
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