Selective Synthesis of a Gasoline Fraction from CO and H2 on a Co-SiO2/ZSM-5/Al2O3 Catalyst

被引:1
作者
Yakovenko, Roman E. [1 ]
Narochnyi, Grigory B. [1 ]
Zubkov, Ivan N. [1 ]
Bozhenko, Ekaterina A. [1 ]
Kataria, Yash V. [1 ]
Svetogorov, Roman D. [2 ]
Savost'yanov, Alexander P. [1 ]
机构
[1] Platov South Russian State Polytech Univ NPI, Res Inst Nanotechnol & New Mat, Prosveschenya 132, Novocherkassk 346428, Russia
[2] Kurchatov Inst, Natl Res Ctr, 1 Akad Kurchatova Sq, Moscow 123098, Russia
关键词
Fischer-Tropsch synthesis; bifunctional cobalt catalyst; HZSM-5; zeolite; synthetic gasoline fuel; FISCHER-TROPSCH SYNTHESIS; BIFUNCTIONAL COBALT CATALYST; ZSM-5; ZEOLITE; MASS-TRANSFER; DIESEL FUEL; HYDROCARBONS; CONVERSION; METHANOL; SYNGAS;
D O I
10.3390/catal13091314
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
This article reports on a simple method for producing high-octane gasoline from CO and H-2 on a Co-Al2O3/SiO2/HZSM-5/Al2O3 hybrid catalyst. In the selected pressure range (0.5, 1.0, and 2.0 MPa), it was found that a decrease in pressure and an increase in temperature contribute to an increase in the content of branched hydrocarbons. The optimal technological parameters of the process were determined to ensure high selectivity and productivity for C-5-C-10 hydrocarbons: pressure-1.0 MPa, ratio H-2/CO = 2, gas space velocity-1000 h(-1), temperature-250( degrees)C. The selectivity for the gasoline fraction is 65.2%, and the ratio of branched to linear hydrocarbons (iso/n index) is 2.3. Under the specified technological conditions, an experimental batch of gasoline fraction (1000 cm(3)) was produced at the pilot plant during 400 h of continuous operation. The main physicochemical and operational parameters of the experimental gasoline fraction of hydrocarbons have been determined. The octane number determined by the research method according to GOST R 52947-2019 is 78.5 units.
引用
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页数:15
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