Chinese Journal of Catalysis ›› 2025, Vol. 73: 222-233.DOI: 10.1016/S1872-2067(25)64682-1
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Wende Hu, Jun Ke, Yangdong Wang(), Chuanming Wang(
)
Received:
2025-01-02
Accepted:
2025-03-18
Online:
2025-06-18
Published:
2025-06-12
Contact:
*E-mail: wangyd.sshy@sinopec.com (Y. Wang),
wangcm.sshy@sinopec.com (C. Wang).
Supported by:
Wende Hu, Jun Ke, Yangdong Wang, Chuanming Wang. First-principles microkinetic simulations revealing the driving effect of zeolite in bifunctional catalysts for the conversion of syngas to olefins[J]. Chinese Journal of Catalysis, 2025, 73: 222-233.
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URL: https://www.cjcatal.com/EN/10.1016/S1872-2067(25)64682-1
Scheme 1. Overview of the primary and secondary reactions in the direct conversion of syngas to light olefins on bifunctional catalysts consisting of oxide and zeolite components.
Scheme 2. Overview of the H2 activation to proton (Olat-H#) and hydride (Zn-H*), the key reactions of WGS, olefin hydrogenation to alkanes, and methanol conversion to methane/DME on ZnAl2O4(111) surface.
Fig. 1. Energy barriers and the corresponding transition state structures of the direct C-O bond scission of different CHxOHy intermediates on ZnAl2O4(111) surface.
Fig. 2. Energy profiles of the formation of methane from methanol (A) and ethane from ethene hydrogenation (B) via different reaction pathways on ZnAl2O4(111) surface at 0 K.
Fig. 5. CO conversion and selectivity to methanol, DME, methane, CO2, olefin and alkane on ZnAl2O4-based bifunctional catalysts with respect to the activity of zeolite component for the conversion of methanol to olefins. Reaction conditions: 673 K, 3 MPa, CO/H2 = 1:2, Flow rate = 10 s-1. It is assumed that the contents of active sites on oxide and zeolite are the same (oxide:zeolite = 1:1).
Fig. 6. Dependence of the CO conversion on the flow rate of reactants and the zeolite activity (P = 3 MPa, A), and the total pressure and the zeolite activity (F = 10 s-1, B) on ZnAl2O4-based bifunctional catalysts. Reaction conditions: 673 K, CO/H2 = 1:2.
Fig. 7. Dependence of the selectivity on the flow rate of reactants and the zeolite activity (P = 3 MPa, A), and the total pressure and the zeolite activity (F = 10 s-1, B) on ZnAl2O4-based bifunctional catalysts. Reaction conditions: 673 K, CO/H2 = 1:2.
Fig. 8. CO conversion and selectivity to methanol, DME, methane, CO2, olefin and alkane on ZnAl2O4-based bifunctional catalysts (oxide:zeolite = 1:1) with respect to the activity of zeolite component for the conversion of methanol to olefins. Reaction conditions: 623 K (A) and 723 K (B), P = 3 MPa, CO/H2 = 1:2, Flow rate = 10 s-1.
Fig. 9. Dependence of the olefin/paraffin ratio on the flow rate of reactants and the zeolite activity (P = 3 MPa, A), and the total pressure and the zeolite activity (F = 10 s-1, B) on ZnAl2O4-based bifunctional catalysts. Reaction conditions: 673 K, CO/H2 = 1:2.
Fig. 10. Relation between the energy barrier of the Concerted hydrogenation and the charge difference of the atoms in the double bond of unsaturated molecules (0 K, A), and the charge density difference of the transition states of the Concerted hydrogenation of formaldehyde and ethene (the iso-surface value is 0.002 a-3, B) on ZnAl2O4(111) surface.
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