Selective Catalytic Reforming of Methane into Synthesis Gas

被引:2
作者
Zhumabek, Manapkhan [1 ,2 ]
Kaumenova, Gulnar [1 ]
Augaliev, Diar [3 ]
Alaidar, Yerbolat [3 ]
Murzin, Dmitry [4 ]
Tungatarova, Svetlana [1 ,3 ]
Xanthopoulou, Galina [5 ]
Kotov, Stanislav [6 ]
Baizhumanova, Tolkyn [1 ,3 ]
机构
[1] DV Sokolsky Inst Fuel Catalysis & Electrochem, 142 Kunaev Str, Alma Ata 050010, Kazakhstan
[2] Satbayev Univ, 22 Satbayev Str, Alma Ata 050013, Kazakhstan
[3] Al Farabi Kazakh Natl Univ, 71 Al Farabi Ave, Alma Ata 050040, Kazakhstan
[4] Abo Akad Univ, 8 Biskopsgatan, Turku 20500, Finland
[5] NCSR Demokritos, Inst Nanosci & Nanotechnol, Aghia Paraskevi 15310, Greece
[6] M Kh Dulaty Taraz Reg Univ, Suleymenov Str 7, Taraz 080012, Kazakhstan
关键词
Catalytic reforming; Hydrogen; Methane; Solution combustion synthesis; Synthesis gas; SOLUTION COMBUSTION SYNTHESIS; PARTIAL OXIDATION; NI; SYNGAS; RU; HYDROTALCITE; CONVERSION; SPINEL; RATIO;
D O I
10.1002/ceat.202100247
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Syngas is an important product of methane processing of natural gas, from which a wide range of chemical products can be obtained in the future. The results of a study of the developed Ni multicomponent catalysts in the partial oxidation of CH4 to syngas are presented. A series of samples with different percentages of active components in a Ni-Cr-Al-Mg-glycine catalyst was prepared by the solution combustion synthesis method giving synthesis gas with a high yield. The optimum conditions for the highest yields of H-2 and CO were identified.
引用
收藏
页码:2026 / 2033
页数:8
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