1. Coke-resistance enhancement of mesoporous γ-Al2O3 and MgO-supported Ni-based catalysts for sustainable hydrogen generation via steam reforming of acetic acid.
- Author
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Ibrahim, Saleh Ahmat, Ekinci, Emine Kaya, Karaman, Birce Pekmezci, and Oktar, Nuray
- Subjects
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STEAM reforming , *INTERSTITIAL hydrogen generation , *ACETIC acid , *CATALYSTS , *CATALYST supports , *CATALYST structure , *MESOPOROUS materials , *NICKEL catalysts - Abstract
Highly ordered mesoporous γ-Al 2 O 3 particles and MgO materials were synthesized by evaporation induced self-assembly (EISA) and template-free hydrothermal co-precipitation routes, respectively. Ni, Ni–MgO, and Ni–La 2 O 3 -containing catalysts were prepared using a wet-impregnation method. The synthesized catalysts were characterized by N 2 adsorption–desorption, XRD, SEM-EDS, DRIFTS, XPS, TGA-DTA, and Raman spectroscopy analysis. The mesoporous γ-Al 2 O 3 catalyst support exhibited a high surface area of 245 m2/g and average pore volume of 0.481 cm3/g. The DRIFTS results indicate the existence of large Lewis's acid regions in the pure γ-Al 2 O 3 and metal-containing catalysts. Catalytic activity tests of pure materials and metal-containing catalysts were carried out at the reaction temperature of 750 °C and a feed molar ratio of AA/H 2 O/Ar:1/2.5/2 over 3 h. Complete conversion of acetic acid and 81.75% hydrogen selectivity were obtained over the catalyst 5Ni@γ-Al 2 O 3. The temperature and feed molar ratio had a noticeable impact on H 2 selectivity and acetic acid conversion. Increasing the water proportion in the feed composition from 2.5 to 10 considerably improved the catalytic activity by increasing hydrogen selectivity from 81.75% to 91%. Although the Ni-based γ-Al 2 O 3 -supported catalysts exhibited higher activity performance compared to the Ni-based MgO-supported catalysts, they were not as resistant to coke formation as were MgO-supported catalysts. The introduction of MgO and La 2 O 3 into the Ni@γ-Al 2 O 3 and Ni@MgO catalysts' structures played a significant role in lowering the carbon formation (from 37.15% to 17.6%–12.44% and 12.17%, respectively) and improving the thermal stability of the catalysts by decreasing the agglomeration of acidic sites and reinforcing the adsorption of CO 2 on the catalysts' surfaces. Therefore, coke deposition was reduced, and catalyst lifetime was improved. • γ-Al 2 O 3 -supported catalysts were active and selective towards H 2 production. • Ni-containing MgO-supported catalysts were stable and resistant to coke deposition. • The catalyst 5Ni–3Mg@γ-Al 2 O 3 was highly active and thermally stable for 12 h. • MgO and La 2 O 3 addition to the Ni-based catalysts lowered coke formation. • Increasing the water proportion in the feedstock favored the reforming reaction. [ABSTRACT FROM AUTHOR]
- Published
- 2021
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