TY - JOUR
T1 - Development of dual-membrane coated Fe/SiO2 catalyst for efficient synthesis of isoparaffins directly from syngas
AU - Jin, Yuzhou
AU - Yang, Guohui
AU - Chen, Qingjun
AU - Niu, Wenqi
AU - Lu, Peng
AU - Yoneyama, Yoshiharu
AU - Tsubaki, Noritatsu
N1 - Publisher Copyright:
© 2014 Elsevier B.V.
PY - 2015/2/1
Y1 - 2015/2/1
N2 - A novel dual-membrane coated catalyst (Fe/SiO2-S-Z) with Fe/SiO2 core and Silicalite-1 and H-ZSM-5 zeolite membranes was developed and employed for isoparaffins direct synthesis from syngas via Fischer-Tropsch synthesis (FTS) reaction. The Silicalite-1 zeolite membrane, as a structural membrane, was prepared under a close-to-neutral synthesis condition, which avoided the structure destruction of the core catalyst Fe/SiO2 and favored the in-situ growth of H-ZSM-5 zeolite membrane. In H-ZSM-5 zeolite membrane, as a functional membrane, the micropores and strong acidic sites were preserved in the dual-membrane catalyst, which played important roles in the isoparaffins direct synthesis. Activity tests indicated that the dual-membrane catalyst exhibited an excellent performance for isoparaffins direct synthesis. The isoparaffins selectivity of the dual-membrane catalyst was up to 29.8%, much higher than those of individual core catalyst (12.9%) and physical mixture catalyst of H-ZSM-5 zeolite and Fe/SiO2 catalyst (16.6%). It was found for the first time that the hydrogenation and isomerization of olefins over the dual-membrane catalyst were the main reasons for the high isoparaffins selectivity. In addition, due to the spatial confinement effect of the microporous zeolite membranes, the hydrocracking and isomerization of heavy hydrocarbons (C12+) also contributed to the high selectivity of isoparaffins.
AB - A novel dual-membrane coated catalyst (Fe/SiO2-S-Z) with Fe/SiO2 core and Silicalite-1 and H-ZSM-5 zeolite membranes was developed and employed for isoparaffins direct synthesis from syngas via Fischer-Tropsch synthesis (FTS) reaction. The Silicalite-1 zeolite membrane, as a structural membrane, was prepared under a close-to-neutral synthesis condition, which avoided the structure destruction of the core catalyst Fe/SiO2 and favored the in-situ growth of H-ZSM-5 zeolite membrane. In H-ZSM-5 zeolite membrane, as a functional membrane, the micropores and strong acidic sites were preserved in the dual-membrane catalyst, which played important roles in the isoparaffins direct synthesis. Activity tests indicated that the dual-membrane catalyst exhibited an excellent performance for isoparaffins direct synthesis. The isoparaffins selectivity of the dual-membrane catalyst was up to 29.8%, much higher than those of individual core catalyst (12.9%) and physical mixture catalyst of H-ZSM-5 zeolite and Fe/SiO2 catalyst (16.6%). It was found for the first time that the hydrogenation and isomerization of olefins over the dual-membrane catalyst were the main reasons for the high isoparaffins selectivity. In addition, due to the spatial confinement effect of the microporous zeolite membranes, the hydrocracking and isomerization of heavy hydrocarbons (C12+) also contributed to the high selectivity of isoparaffins.
KW - Dual-membrane catalyst
KW - Fischer-Tropsch Synthesis (FTS)
KW - H-ZSM-5 zeolite membrane
KW - Isoparaffins synthesis
KW - Silicalite-1 zeolite membrane
UR - http://www.scopus.com/inward/record.url?scp=84908351443&partnerID=8YFLogxK
U2 - 10.1016/j.memsci.2014.10.004
DO - 10.1016/j.memsci.2014.10.004
M3 - 学術論文
AN - SCOPUS:84908351443
SN - 0376-7388
VL - 475
SP - 22
EP - 29
JO - Journal of Membrane Science
JF - Journal of Membrane Science
ER -