2021
DOI: 10.1016/j.ijhydene.2020.11.250
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High-purity hydrogen production by sorption-enhanced methanol steam reforming over a combination of Cu–Zn–CeO2–ZrO2/MCM-41 catalyst and (Li–Na–K) NO3·MgO adsorbent

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Cited by 33 publications
(12 citation statements)
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“…The proposed modifications of the catalysts are most broadly related to the improvement of the dispersion of copper particles and the enhancement of their redox properties [68]. Among promoters for copper catalysts, ZrO 2 [68,69], Ga 2 O 3 [73], TiO 2 [66], ZnO [71], CeO 2 [57,68,74], MgO [71,75], yttrium [72], lithium, sodium potassium [75], and lanthanum [76] have been reported. The amount of promoter added to the catalyst structure strongly affects the catalytic activity; therefore, the selection of the appropriate promoter content is crucial for the activity and selectivity of the methanol steam reforming process.…”
Section: Hydrogen Generation From Methanolmentioning
confidence: 99%
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“…The proposed modifications of the catalysts are most broadly related to the improvement of the dispersion of copper particles and the enhancement of their redox properties [68]. Among promoters for copper catalysts, ZrO 2 [68,69], Ga 2 O 3 [73], TiO 2 [66], ZnO [71], CeO 2 [57,68,74], MgO [71,75], yttrium [72], lithium, sodium potassium [75], and lanthanum [76] have been reported. The amount of promoter added to the catalyst structure strongly affects the catalytic activity; therefore, the selection of the appropriate promoter content is crucial for the activity and selectivity of the methanol steam reforming process.…”
Section: Hydrogen Generation From Methanolmentioning
confidence: 99%
“…Moreover, the addition of titanium promotes the reduction of the acidity of the catalyst, thus limiting the occurrence of side reactions. It was also reported that a basic promoter, including Na, K, Mg, may be used as a sorbent for generated carbon dioxide, allowing for obtaining a gas stream with an even higher hydrogen content [75].…”
Section: Hydrogen Generation From Methanolmentioning
confidence: 99%
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“…18 Therefore, the development of a feasible pathway to simultaneously improve the hydrogen concentration and lower the CO selectivity, through which the thermodynamic equilibria of both SRM and WGS can be promoted by in situ CO 2 adsorption. 21,22 A few experimental studies have been conducted to verify the feasibility of SE-SRM by using intermediate-temperature CO 2 sorbents such as MgO and hydrotalcite. Wu et al 23 investigated the hydrogen production characteristics of SE-SRM at 230 C under atmospheric pressure, using commercial CuO/ZnO/Al 2 O 3 and K 2 CO 3 -modied hydrotalcite as a catalyst and CO 2 sorbent, respectively.…”
Section: Introductionmentioning
confidence: 99%
“…Hydrogen is essentially produced by methanol steam reforming according to Equation (1). This overall reaction is accompanied by other side reactions such as methanol decomposition (Equation ( 2)) and water gas-shift reaction (Equation (3)), as follows [5]:…”
Section: Introductionmentioning
confidence: 99%