TY - JOUR
T1 - H-type zeolite coated iron-based multiple-functional catalyst for direct synthesis of middle isoparaffins from syngas
AU - Bao, Jun
AU - Yang, Guohui
AU - Okada, Chie
AU - Yoneyama, Yoshiharu
AU - Tsubaki, Noritatsu
N1 - Funding Information:
This work was supported by Venture Business Laboratory, University of Toyama , Japan; Japan Oil, Gas and Metals National Corporation as well as Nippon Oil Corporation .
PY - 2011/2/28
Y1 - 2011/2/28
N2 - A compact, integral zeolite shell of H-ZSM-5 was directly crystallized on the surface of fused-iron catalyst pellet by a hydrothermal synthesis method. The synthesized catalyst has a core-shell structure without pinholes and cracks. For the reaction of direct synthesis of isoparaffin from syngas, the formation of C10+ hydrocarbons is suppressed completely on this core-shell catalyst, and the middle isoparaffins become the main products. Especially, desirable low methane selectivity is achieved. The core-shell structure of the catalyst provides a tailor-made confined reaction environment with spatially confined effect and shape selectivity, where isoparaffins escaping from outer surface of one core-shell catalyst hardly enter another core-shell catalyst via surface zeolite shell, due to its large steric obstacle, ensuring the elevated isoparaffin selectivity. Furthermore, this type of core-shell catalyst has very high membrane area per unit reactor volume and easy to be prepared, in contrast to the conventional membrane reactor.
AB - A compact, integral zeolite shell of H-ZSM-5 was directly crystallized on the surface of fused-iron catalyst pellet by a hydrothermal synthesis method. The synthesized catalyst has a core-shell structure without pinholes and cracks. For the reaction of direct synthesis of isoparaffin from syngas, the formation of C10+ hydrocarbons is suppressed completely on this core-shell catalyst, and the middle isoparaffins become the main products. Especially, desirable low methane selectivity is achieved. The core-shell structure of the catalyst provides a tailor-made confined reaction environment with spatially confined effect and shape selectivity, where isoparaffins escaping from outer surface of one core-shell catalyst hardly enter another core-shell catalyst via surface zeolite shell, due to its large steric obstacle, ensuring the elevated isoparaffin selectivity. Furthermore, this type of core-shell catalyst has very high membrane area per unit reactor volume and easy to be prepared, in contrast to the conventional membrane reactor.
KW - Core-shell structure
KW - H-ZSM-5 zeolite
KW - Isoparaffin synthesis
KW - Shape selectivity
KW - Spatially confined effect
UR - http://www.scopus.com/inward/record.url?scp=79951670781&partnerID=8YFLogxK
U2 - 10.1016/j.apcata.2010.12.041
DO - 10.1016/j.apcata.2010.12.041
M3 - 学術論文
AN - SCOPUS:79951670781
SN - 0926-860X
VL - 394
SP - 195
EP - 200
JO - Applied Catalysis A: General
JF - Applied Catalysis A: General
IS - 1-2
ER -