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Steam reforming of shale gas in a packed bed reactor with and without chemical looping using nickel based oxygen carrier

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Figure

Table 2 e Comparison of CL-SR with C-SR process and
Table 3 e CL-SR process characterization results at 1 bar, GHSV 0.498 and S:C 3. For CL-SR Reforming/reduction reaction at750 �C and oxidation reaction at 750 �C
Fig. 2 econversion using 18 wt. % NiO on Al650 Effect of GHSV on H2 yield and purity, fuel and H2O2O3 support at 1 bar, �C and S:C 3 (average values).
Fig. 3 eGHSV 0.498 and S:C 3 (a) using 18 wt. % NiO on Al Comparative analysis between experimental (average) process output and chemical equilibrium results at 1 bar,2O3 support catalyst (b) using 15 wt
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