Hydrogen production from bio-ethanol steam reforming reaction in a Pd/PSS membrane reactor

Effects of Catalysts and Membranes on the Performance of Membrane Reactors in Steam Reforming of Ethanol at Moderate Temperature

“…This means the selective H 2 removal through Pd 77 Ag 23 membrane kinetically inhibited the methane production, resulting in high H 2 yield at low reaction temperature. Indeed, Seelam et al reported Co/Al 2 O 2 that showed high membrane performance at 673 K compared to Ni/ZrO 2 because of high methane selectivity in Ni/ZrO 2 [27], which is consistent with our experimental results. …”

Advances in Ethanol Reforming for the Production of Hydrogen

“…Using a similar approach, Seelam et al 69 explored the SRE in a reactor with a platinum-based membrane supported on stainless steel. The experiment was performed with two catalysts: Ni/ZrO 2 and Co/Al 2 O 3 .…”

The oncoming energy vector: Hydrogen produced in Pd-composite membrane reactor via bioethanol reforming over Ni/CeO 2 catalyst

“…Therefore, in the last years ESR reaction in composite Pd-based MRs has been particularly investigated [26,[29][30][31][32]43]. In particular, Papadias et al [26] used a supported Pd/Ag MR (30 m as metallic layer) packed with Rh-LaAl 2 O 3 catalyst.…”

“…In order to intensify the whole process and generate high grade hydrogen, a Pd-based MR could represent an alternative to the conventional systems to carry out ESR reaction [26][27][28][29][30][31][32][33][34][35][36][37][38][39][40][41][42][43]. Indeed, several scientific papers demonstrated the feasibility of this device toward realistic improvements of the reforming process in terms of hydrogen production and costs reduction [21,[26][27][28][29][30][31][32].…”