Effect of potassium in catalysts obtained by the solution combustion synthesis for co-production of hydrogen and carbon nanofibers by catalytic decomposition of methane

被引:11
作者
Chudakova, M. V. [1 ]
Popov, M. V. [1 ]
Korovchenko, P. A. [1 ]
Pentsak, E. O. [2 ]
Latypova, A. R. [2 ]
Kurmashov, P. B. [3 ]
Pimenov, A. A. [4 ]
Tsilimbaeva, E. A. [5 ]
Levin, I. S. [6 ]
Bannov, A. G. [3 ,8 ]
Kleymenov, A. V. [7 ]
机构
[1] Gazpromneft Ind Innovat LLC, St Petersburg 197350, Russia
[2] RAS, ND Zelinsky Inst Organ Chem, Moscow 119991, Russia
[3] Novosibirsk State Tech Univ, Novosibirsk 630073, Russia
[4] Gazprom VNIIGAZ LLC, Moscow 142717, Russia
[5] Samara State Tech Univ, Chem Dept, Samara 443100, Russia
[6] RAS, AV Topchiev Inst Petrochem Synth, TIPS RAS, Moscow 119991, Russia
[7] Gazprom Neft PJSC, St Petersburg 190000, Russia
[8] Novosibirsk State Tech Univ, K Marx Ave 20, Novosibirsk 630087, Russia
关键词
Nickel-based catalyst; Potassium promoter; Solution combustion synthesis; Methane decomposition; Hydrogen; Carbon nanofibers; COX-FREE HYDROGEN; NI-BASED CATALYSTS; BIMETALLIC CATALYSTS; NI/SIO2; CATALYSTS; FREE H-2; PYROLYSIS; NANOTUBES; PERFORMANCE; CONVERSION; EROSION;
D O I
10.1016/j.ces.2023.119408
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A set of catalysts containing 0.25-10 wt% K2O was prepared by solution combustion synthesis. The catalytic systems were characterized by X-ray diffraction, transmission electron microscopy, scanning electron microscopy, and low-temperature nitrogen adsorption. The catalytic methane decomposition was carried out at 0.5 MPa, 100 LCH4/(h & sdot;gcat), and temperature ranging from 550 to 750 degrees C. It has been found that varying the potassium content led to a change in the phase composition and textural characteristics of the resulting catalysts. The introduction of potassium (0.25 wt% K2O) into the nickel catalyst made it possible to change the particle size distribution towards the formation of smaller particles, from 5 to 30 nm to 5-10 nm, promoting the formation of higher yield of H2. The Ni-0.25 %K2O/Al2O3 i Ni-1 %K2O/Al2O3 catalysts demonstrated the highest hydrogen yield of 11.6 g/gcat and 17.0 g/gcat with a maximum at 675 and 750 degrees C, respectively. The highest yield of carbon material (51.0 g/gcat) was obtained over Ni-1 %K2O/Al2O3 catalyst.
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页数:14
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