One-step conversion of syngas to light olefins over bifunctional metal-zeolite catalyst
Catalysis, Kinetics and Reaction Engineering|Updated:2026-01-06
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One-step conversion of syngas to light olefins over bifunctional metal-zeolite catalyst
Chinese Journal of Chemical EngineeringVol. 36, Issue 8, Pages: 101-110(2021)
Affiliations:
1. Zhejiang Provincial Key Lab for Chem. & Bio. Processing Technology of Farm Product, School of Biological and Chemical Engineering, Zhejiang University of Science and Technology,Hangzhou,China,310023
2. Department of Applied Chemistry, School of Engineering, University of Toyama, Gofuku 3190,Toyama,Japan,930-8555
3. State Key Laboratory Cultivation Base of Natural Gas Conversion, Ningxia University,Yinchuan,China,750021
Author bio:
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Published:2021
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Ce Du, Linet Gapu Chizema, Emmerson Hondo, Mingliang Tong, Qingxiang Ma, Xinhua Gao, Ruiqin Yang, Peng Lu, Noritatsu Tsubaki. One-step conversion of syngas to light olefins over bifunctional metal-zeolite catalyst[J]. Chinese Journal of Chemical Engineering, 2021, 36(8): 101-110.
DOI:
Ce Du, Linet Gapu Chizema, Emmerson Hondo, Mingliang Tong, Qingxiang Ma, Xinhua Gao, Ruiqin Yang, Peng Lu, Noritatsu Tsubaki. One-step conversion of syngas to light olefins over bifunctional metal-zeolite catalyst[J]. Chinese Journal of Chemical Engineering, 2021, 36(8): 101-110.DOI:
One-step conversion of syngas to light olefins over bifunctional metal-zeolite catalyst
) are fundamental building blocks for the manufacture of polymers
chemical intermediates
and solvents. In this work
we realized a composite catalyst
comprising Mn
x
Zr
y
oxides and SAPO-34 zeolite
which can convert syngas (CO + H
2
) into light olefins. Mn
x
Zr
y
oxide catalysts with different Mn/Zr molar ratios were facilely prepared using the coprecipitation method prior to physical mixing with SAPO-34 zeolite. The redox properties
surface morphology
electronic state
crystal structure
and chemical elemental composition of the catalysts were examined using H
2
-TPR
SEM
XPS
XRD
and EDS techniques
respectively. Tandem reactions involved activation of CO and subsequent hydrogenation over the metal oxide catalyst
producing methanol and dimethyl ether as the main reaction intermediates
which then migrated onto SAPO-34 zeolite for light olefins synthesis. Effects of temperature
pressure and reactant gas flow rate on CO conversion and light olefins selectivity were investigated in detail. The Mn
1
Zr
2
/SAPO-34 catalyst (Mn/Zr ra
tio of 1:2) attained a CO conversion of 10.8% and light olefins selectivity of 60.7%
at an optimized temperature
pressure and GHSV of 380 ℃
3 MPa and 3000 h
-1
respectively. These findings open avenues to exploit other metal oxides with CO activation capabilities for a more efficient syngas conversion and product selectivity.
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Highly efficient cleavage of CO bonds in diphenyl ether over Ni-S2O82-/ZrO2 solid super acid catalysts
Synergistic effect of Co0 with Cu11In9 intermetallic compound enhancing catalytic performance of CO2 hydrogenation to methanol
Effect of carbon modifications on the performance of hydrogenation catalysts
Enhanced activity and stability of SAPO-5 zeolite supported RuMn catalyst for aqueous-phase selective hydrodeoxygenation of guaiacol to cyclohexanol
Toward the rational design for low-temperature hydrogenation of silicon tetrachloride: Mechanism and data-driven interpretable descriptor
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