Production of Gaseous Olefins from Syngas over a Cobalt-HZSM-5 Catalyst

被引:9
|
作者
Maddi, Balakrishna [1 ,2 ]
Davidson, Stephen [2 ]
Job, Heather [2 ]
Dagle, Robert [2 ]
Guo, Mond [2 ]
Gray, Michel [2 ]
Ramasamy, Karthikeyan K. [2 ]
机构
[1] Univ Toledo, Chem & Environm Engn, 2801 W Bancroft St, Toledo, OH 43606 USA
[2] Pacific Northwest Natl Lab, 902 Battelle Blvd, Richland, WA 99354 USA
关键词
Syngas hydrogenation; Unconventional fossil feedstocks; Biofuels; Cobalt; Zeolite; Applied catalysis; FISCHER-TROPSCH SYNTHESIS; BIOMASS-DERIVED SYNGAS; LIGHT OLEFINS; H-ZSM-5-SUPPORTED COBALT; TECHNOECONOMIC ANALYSIS; ACTIVATED-CARBON; IRON CATALYSTS; ISO-PARAFFINS; HYDROCARBONS; CONVERSION;
D O I
10.1007/s10562-020-03324-7
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Light olefins (C-2-C-5) are high-value platform chemicals used to produce plastics, lubricants, coating material, and surfactants, and can be intermediates to produce transportation fuels. In this study we report on the development of a Co-based catalyst for direct conversion of fossil as well as biomass derived syngas into light olefins that enables high conversion and olefin/paraffin (O/P) product ratio, minimal selectivity to CO2 (< 1%) and wax formation (C14+ selectivity < 1%). Over a Co/HZSM-5 bi-functional catalyst 38% CO conversion with C-2-C-5 olefin selectivity of 48%, and O/P ratio of 4.0 was achieved at 240 degrees C, 17 bar, and 1.5 L/(g-h). In addition to a gaseous olefin-rich stream a C-6-C-13 mixed olefin/paraffin liquid byproduct was also produced with 25% selectivity. Both Co loading and the HZSM-5 acidity levels were optimized to maintain the balance between the hydrogenation and the cracking activity to generate high levels of C-2-C-4 olefins. A suite of catalyst characterization tools were used to correlate the physical and chemical property of the catalyst to the performance of the catalyst towards syngas conversion and C-2-C-4 olefin selectivity. [GRAPHICS] .
引用
收藏
页码:526 / 537
页数:12
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