Ni–Al layered double hydroxides as catalyst precursors for CO2 removal by methanation
The effect of nickel content on the structure and activity of co-precipitated Ni–Al layered double hydroxides (LDHs) as catalyst precursors for CO 2 removal by methanation was studied by variation of the Ni 2+ /Al 3+ molar ratio (Ni 2+ /Al 3+ = 3.0, 1.5 and 0.5), and of the reduction and reaction t...
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Veröffentlicht in: | Reaction kinetics, mechanisms and catalysis mechanisms and catalysis, 2012-02, Vol.105 (1), p.79-99 |
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Sprache: | eng |
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Zusammenfassung: | The effect of nickel content on the structure and activity of co-precipitated Ni–Al layered double hydroxides (LDHs) as catalyst precursors for CO
2
removal by methanation was studied by variation of the Ni
2+
/Al
3+
molar ratio (Ni
2+
/Al
3+
= 3.0, 1.5 and 0.5), and of the reduction and reaction temperatures as well as of the space velocities. Powder X-ray diffraction (PXRD), H
2
chemisorption, and temperature programmed reduction (TPR) techniques were applied for physicochemical characterization of the samples. It was specified that the nano-scaled dimensions of the as-synthesized samples also generate nano-metrical metallic nickel particles (PXRD). The existence of readily and hardly reducible Ni
2+
–O species in the studied samples (TPR), affects catalytic performance. The studied catalysts hydrogenate CO
2
effectively to residual concentrations of the latter in the range of 0–10 ppm at reaction temperatures from 400 to 220 °C and space velocities between 22,000 and 3000 h
−1
. The variation of the CO
2
methanation activity with the changes of space velocities depends on the nickel content, and reduction and reaction temperatures. After reduction at 400 and 450 °C, a sample of Ni
2+
/Al
3+
= 3.0 has demonstrated the highest conversion degree at all the reaction temperatures and space velocities, while a catalyst of Ni
2+
/Al
3+
= 0.5 dominated in the methanation activity after reduction within 530–600 °C. The Ni
2+
/Al
3+
= 1.5 catalyst data take intermediate position between Ni
2+
/Al
3+
= 3.0 and Ni
2+
/Al
3+
= 0.5 often closer to Ni
2+
/Al
3+
= 3.0 ones. The studied Ni–Al LDH systems are found to be promising catalyst precursors for fine CO
2
removal from hydrogen-rich gas streams through the methanation reaction, depending on the technological regime of catalyst activation. |
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ISSN: | 1878-5190 1878-5204 |
DOI: | 10.1007/s11144-011-0378-0 |