TY - JOUR
T1 - Direct conversion of carbon dioxide into liquefied petroleum gas over zeolite capsule catalyst
AU - Zhang, Peipei
AU - Huang, Xin
AU - Qu, Shunli
AU - Wang, Peng
AU - Mi, Xiaotong
AU - Li, Sixuan
AU - Xiang, Wenjie
AU - Huang, Hao
AU - Liu, Guangbo
AU - Tsubaki, Noritatsu
AU - Tan, Li
N1 - Publisher Copyright:
© The Author(s), under exclusive licence to Springer Nature B.V. 2025.
PY - 2025/2
Y1 - 2025/2
N2 - The use of bifunctional catalysts, combining methanol synthesis and zeolite components, has been cleverly expanding to the hydrogenation of CO2 into liquefied petroleum gas (LPG). However, such catalysts in this reaction displayed low catalytic efficiency due to the mismatch of the two components. In this study, an efficient strategy was realized via physically coating β zeolite onto the CuZnAl methanol catalyst, resulting in a shell thickness controllable core–shell encapsulated catalyst, denoted as CuZnAl@β. Sufficient characterization proves that the micro-coupling structure between methanol active sites and zeolite acid sites is designed reasonably and successfully, as consequently, the zeolite capsule catalysts embody a significant improvement toward LPG selectivity. Hence, the CuZnAl@β catalyst reached a high selectivity to LPG at 77.9% with 21.3% CO2 conversion, under a reaction pressure of 2.0 MPa and a temperature of 320 °C. The strategy employed in this study could offer valuable insights into guiding catalyst design.
AB - The use of bifunctional catalysts, combining methanol synthesis and zeolite components, has been cleverly expanding to the hydrogenation of CO2 into liquefied petroleum gas (LPG). However, such catalysts in this reaction displayed low catalytic efficiency due to the mismatch of the two components. In this study, an efficient strategy was realized via physically coating β zeolite onto the CuZnAl methanol catalyst, resulting in a shell thickness controllable core–shell encapsulated catalyst, denoted as CuZnAl@β. Sufficient characterization proves that the micro-coupling structure between methanol active sites and zeolite acid sites is designed reasonably and successfully, as consequently, the zeolite capsule catalysts embody a significant improvement toward LPG selectivity. Hence, the CuZnAl@β catalyst reached a high selectivity to LPG at 77.9% with 21.3% CO2 conversion, under a reaction pressure of 2.0 MPa and a temperature of 320 °C. The strategy employed in this study could offer valuable insights into guiding catalyst design.
KW - Bifunctional active sites
KW - CO hydrogenation
KW - Capsule catalyst
KW - Liquefied petroleum gas
KW - β zeolite
UR - http://www.scopus.com/inward/record.url?scp=85213985796&partnerID=8YFLogxK
U2 - 10.1007/s11164-024-05488-y
DO - 10.1007/s11164-024-05488-y
M3 - 学術論文
AN - SCOPUS:85213985796
SN - 0922-6168
VL - 51
SP - 675
EP - 693
JO - Research on Chemical Intermediates
JF - Research on Chemical Intermediates
IS - 2
M1 - 100445
ER -