2018
DOI: 10.1021/acs.iecr.8b02488
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Interplay of support chemistry and reaction conditions on copper catalyzed methanol steam reforming

Abstract: A series of Cu catalysts supported on SiO2, Al2O3–SiO2, TiO2 rutile, and Cu/TiO2 anatase metal oxides has been studied for methanol reforming in the vapor phase. The highest activity was obtained on Cu/SiO2 catalysts (5493 μmol H2 min–1·gcat–1) followed by Cu/TiO2 rutile, Cu/Al2O3–SiO2, and anatase. XRD and HRTEM characterization after reaction revealed that on Cu/SiO2 significant sintering occurred during reaction. In contrast, the particle size growth on Cu/TiO2 rutile and anatase was less pronounced, which … Show more

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Cited by 18 publications
(21 citation statements)
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“…Cu/Al 2 O 3 −SiO 2 was deactivated rather early due to coke formation. 110 Apart from Al, promoters such as ZrO 2 and CeO 2 have also been reported. Lindstrom and Pettersson investigated various alumina-supported monolithic copper-based catalysts with and without zirconia doping.…”
Section: Cu-based Catalystsmentioning
confidence: 99%
See 1 more Smart Citation
“…Cu/Al 2 O 3 −SiO 2 was deactivated rather early due to coke formation. 110 Apart from Al, promoters such as ZrO 2 and CeO 2 have also been reported. Lindstrom and Pettersson investigated various alumina-supported monolithic copper-based catalysts with and without zirconia doping.…”
Section: Cu-based Catalystsmentioning
confidence: 99%
“…Cu/SiO 2 suffered from significant sintering during the reaction, while Cu/TiO 2 -rutile and -anatase had restricted particle size growth. Cu/Al 2 O 3 –SiO 2 was deactivated rather early due to coke formation …”
Section: Cu-based Catalystsmentioning
confidence: 99%
“…However, the main drawback of copper-based catalysts in the SRM is their catalytic deactivation due to the formation of coke at high temperatures [14], which covers the surface of the catalyst. In comparison with copper-based catalysts, the reports on Ru [15], Pt [16], and Pd [17] indicate that noble metal catalysts have inherently higher selectivity for methanol decompo-sition, resulting in higher CO production, but better long-term thermal stability in the SRM [5,8].…”
Section: Introductionmentioning
confidence: 99%
“…As an ideal liquid fuel, methanol has a wide variety of sources, lower price, easy to store and transport, and has higher energy density. Therefore, the methanol can be favoured transformed to hydrogen by catalytic reforming reaction at relatively low temperatures (200-300℃) [1][2][3][4]. At present, the mainly applied methods of hydrogen production from methanol contained partial oxidation of methanol (POM) and steam reforming of methanol (SRM) [5].…”
Section: Introductionmentioning
confidence: 99%
“…CuO/ZnO/Al2O3 catalysts were widely used in steam reforming of methanol [8,9], because of its excellent performance during low temperature range and select hydrogen selectivity [3]. The mainly preparation methods for CuO/ZnO/Al2O3 catalysts were co-precipitation and hydrothermal methods.…”
Section: Introductionmentioning
confidence: 99%