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Modelling of high purity H2 production via sorption enhanced chemical looping steam reforming of methane in a packed bed reactor

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Academic year: 2019

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Figure

Figure 1: The schematic of SE-CLSR process in packed bed.  = closed & = open valves
Figure 2: The effect of pressure on a) CH4 conversion; b) H2 purity; c) H2 yield (wt. % of CH4) and d) CO2
Figure 3: The effect of temperature on the a) CH4 conversion; b) H2 purity; c) H2 yield (wt
Figure 4: Effect of CaO/C on the a) CH4 conversion; CO2 capturing efficiency; b) H2 purity; and c) H2 yield (wt
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