One-step conversion of syngas to light olefins over bifunctional metal-zeolite catalyst

被引:12
作者
Du, Ce [1 ,2 ]
Chizema, Linet Gapu [1 ]
Hondo, Emmerson [1 ]
Tong, Mingliang [1 ]
Ma, Qingxiang [3 ]
Gao, Xinhua [3 ]
Yang, Ruiqin [1 ]
Lu, Peng [1 ]
Tsubaki, Noritatsu [2 ]
机构
[1] Zhejiang Univ Sci & Technol, Sch Biol & Chem Engn, Zhejiang Prov Key Lab Chem & Bio Proc Technol Far, Hangzhou 310023, Peoples R China
[2] Univ Toyama, Sch Engn, Dept Appl Chem, Gofuku 3190, Toyama 9308555, Japan
[3] Ningxia Univ, State Key Lab Cultivat Base Nat Gas Convers, Yinchuan 750021, Ningxia, Peoples R China
来源
CHINESE JOURNAL OF CHEMICAL ENGINEERING | 2021年 / 36卷
关键词
Catalyst; C-C coupling; CO activation; Hydrogenation; Light olefins; Syngas; MN-ZR OXIDES; TOTAL OXIDATION; HYDROGENATION; PERFORMANCE; ZIRCONIUM; DESIGN; GAS; CO; SELECTIVITY; REDUCTION;
D O I
10.1016/j.cjche.2020.09.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Light olefins (C-2-C-4) are fundamental building blocks for the manufacture of polymers, chemical intermediates, and solvents. In this work, we realized a composite catalyst, comprising MnxZry oxides and SAPO-34 zeolite, which can convert syngas (CO + H-2) into light olefins. MnxZry 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 Mn1Zr2/SAPO-34 catalyst (Mn/Zr ratio 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 degrees C, 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. (C) 2020 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:101 / 110
页数:10
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