TY - JOUR
T1 - Monolithic metal-fiber@HZSM-5 core-shell catalysts for methanol-to-propylene
AU - Wen, Ming
AU - Wang, Xiangyu
AU - Han, Lupeng
AU - Ding, Jia
AU - Sun, Ying
AU - Liu, Ye
AU - Lu, Yong
N1 - Publisher Copyright:
© 2014 Elsevier Inc. All rights reserved.
PY - 2015/4/1
Y1 - 2015/4/1
N2 - Monolithic metal-fiber@HZSM-5 core-shell catalysts have been developed by direct growth of zeolite crystals on a macroscopic 3D network of sinter-locked metal microfibers. This approach provides a combination of excellent thermal conductivity, hierarchical porous structure from micro- to macro-size, and unique form factor. The metal-fiber@HZSM-5 catalysts, with high HZSM-5 loadings (e.g., 27-30 wt%) and excellent core-shell robustness, deliver dramatic selectivity and life-time improvement in the methanol-to-olefin process. Such unprecedented performance is due to propagation of the olefin methylation/cracking cycle over the aromatic-based cycle in the methanol-to-hydrocarbon catalysis. Using a feed of 30 vol% methanol in N2, for example, at 480 °C high propylene selectivity of ∼46% can be obtainable with a total C2-C4 olefin selectivity of ∼70%, being much higher than that (∼37%, C2-C4 olefin selectivity of ∼64%) for the corresponding zeolite powder. The core-shell catalyst is stable at least for 210 h, almost 3-fold longer than the life-time of 60 h for the powdered HZSM-5 catalysts, because the coking rate is obviously suppressed in association with the propagated olefin-based cycle.
AB - Monolithic metal-fiber@HZSM-5 core-shell catalysts have been developed by direct growth of zeolite crystals on a macroscopic 3D network of sinter-locked metal microfibers. This approach provides a combination of excellent thermal conductivity, hierarchical porous structure from micro- to macro-size, and unique form factor. The metal-fiber@HZSM-5 catalysts, with high HZSM-5 loadings (e.g., 27-30 wt%) and excellent core-shell robustness, deliver dramatic selectivity and life-time improvement in the methanol-to-olefin process. Such unprecedented performance is due to propagation of the olefin methylation/cracking cycle over the aromatic-based cycle in the methanol-to-hydrocarbon catalysis. Using a feed of 30 vol% methanol in N2, for example, at 480 °C high propylene selectivity of ∼46% can be obtainable with a total C2-C4 olefin selectivity of ∼70%, being much higher than that (∼37%, C2-C4 olefin selectivity of ∼64%) for the corresponding zeolite powder. The core-shell catalyst is stable at least for 210 h, almost 3-fold longer than the life-time of 60 h for the powdered HZSM-5 catalysts, because the coking rate is obviously suppressed in association with the propagated olefin-based cycle.
KW - Core-shell structure
KW - Metal fiber
KW - Methanol to propylene
KW - Structured catalyst
KW - ZSM-5 zeolite
UR - https://www.scopus.com/pages/publications/84922167559
U2 - 10.1016/j.micromeso.2014.12.007
DO - 10.1016/j.micromeso.2014.12.007
M3 - 文章
AN - SCOPUS:84922167559
SN - 1387-1811
VL - 206
SP - 8
EP - 16
JO - Microporous and Mesoporous Materials
JF - Microporous and Mesoporous Materials
IS - C
ER -