TY - JOUR
T1 - Uniform silica-infused ZIF-67 derived Fischer−Tropsch cobalt catalyst integrated with ZSM-5 for sustainable aviation fuel synthesis
AU - Chen, Guoqing
AU - Ma, Zhongchen
AU - Gu, Wenli
AU - Liu, Pu
AU - Lan, Tian
AU - Lu, Yong
N1 - Publisher Copyright:
© 2026 Elsevier B.V.
PY - 2026/3/15
Y1 - 2026/3/15
N2 - The direct production of sustainable aviation fuel (SAF) through Fischer−Tropsch synthesis (FTS) has garnered significant interest within the energy and petrochemical sectors. However, attaining high SAF selectivity remains a critical hurdle, as the inherent maximum selectivity for the C8−C16 hydrocarbon fraction in traditional FTS process hovers around 41%. Here, we report a promising bifunctional catalyst system for FTS to SAF, featuring cobalt nanoparticles (Co NPs) embedded within amorphous silica (Co@xSi) integrated with ZSM-5 zeolite. The optimal catalyst system was identified by combining Co@3Si derived from an APTES-infused ZIF-67 (with a 3:1 mass ratio of APTES to ZIF-67) with two mass fractions of a ZSM-5 (Co@3Si&2Z5). This formulation achieved a 75.2% selectivity to C8−C16 hydrocarbons with an iso-paraffins proportion of 24.3%, while effectively minimizing CH4 formation to 6.3%. It also sustained a high CO conversion of 85.1% and was stable for at least 168 h. The Co@3Si, leveraging its abundant active cobalt sites and distinctive confined structure, not only improved CO adsorption and activation but also extended the residence time of −CHx intermediates on the surface of Co NPs, thereby efficiently facilitating the formation of long-chain hydrocarbons. The ZSM-5 zeolite facilitated the selective catalytic cracking and isomerization of long-chain hydrocarbons, effectively converting them into SAF-range paraffins. The collaborative synergy between the two core components forms an efficient catalytic process akin to an assembly line, enabling the highly selective direct transformation of syngas into SAF.
AB - The direct production of sustainable aviation fuel (SAF) through Fischer−Tropsch synthesis (FTS) has garnered significant interest within the energy and petrochemical sectors. However, attaining high SAF selectivity remains a critical hurdle, as the inherent maximum selectivity for the C8−C16 hydrocarbon fraction in traditional FTS process hovers around 41%. Here, we report a promising bifunctional catalyst system for FTS to SAF, featuring cobalt nanoparticles (Co NPs) embedded within amorphous silica (Co@xSi) integrated with ZSM-5 zeolite. The optimal catalyst system was identified by combining Co@3Si derived from an APTES-infused ZIF-67 (with a 3:1 mass ratio of APTES to ZIF-67) with two mass fractions of a ZSM-5 (Co@3Si&2Z5). This formulation achieved a 75.2% selectivity to C8−C16 hydrocarbons with an iso-paraffins proportion of 24.3%, while effectively minimizing CH4 formation to 6.3%. It also sustained a high CO conversion of 85.1% and was stable for at least 168 h. The Co@3Si, leveraging its abundant active cobalt sites and distinctive confined structure, not only improved CO adsorption and activation but also extended the residence time of −CHx intermediates on the surface of Co NPs, thereby efficiently facilitating the formation of long-chain hydrocarbons. The ZSM-5 zeolite facilitated the selective catalytic cracking and isomerization of long-chain hydrocarbons, effectively converting them into SAF-range paraffins. The collaborative synergy between the two core components forms an efficient catalytic process akin to an assembly line, enabling the highly selective direct transformation of syngas into SAF.
KW - Cobalt
KW - Fischer−Tropsch synthesis
KW - Sustainable aviation fuel
KW - ZIF-67
KW - ZSM-5
UR - https://www.scopus.com/pages/publications/105030653167
U2 - 10.1016/j.cej.2026.174364
DO - 10.1016/j.cej.2026.174364
M3 - 文章
AN - SCOPUS:105030653167
SN - 1385-8947
VL - 532
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 174364
ER -