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Continuous hydrogen production by sorption enhanced steam methane reforming (SE-SMR) has been studied using a circulating fluidized bed reactor with calcined natural dolomite as CO 2 sorbent and Ni/NiAl 2 O 4 as catalyst. A steam to methane ratio of 4 was used at 575°C and ambient pressure. Two experiments, each run for 8h, were carried out using two different volumetric catalyst...
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