The three main reaction stages of a H 2 production process based on the combination of the CaO/CaCO 3 and Cu/CuO loops have been experimentally studied in a lab scale fixed bed reactor. The solid bed contained the three functional materials required to run the process, namely a commercial Ni-based catalyst, a CaO-Ca 12 Al 14 O 33 CO 2 sorbent and a CuO-Al 2 O 3 material in a proportion that resulted in a bed with 43.3 % wt. CuO, 25.6 % wt. CaO and 1.7 % wt. Ni. The system was able to convert 13.5 kg CH 4 h-1 kg Ni-1 , at 675 ºC producing a gas stream with a 93.5 % vol. H 2 at 10 bar. The Cu-based material presented high oxidation kinetics, being totally converted in a narrow reaction front with a highly diluted air stream at 10 bar. The Cu-based material presented also fast reduction kinetics and it was completely converted with a fuel gas with typical composition of a SMR stage at high temperature. A Cu/Ca molar ratio of 2 allowed for calcination efficiencies over 85 % molar basis at the CO and H 2 breakthrough , and 95 % of the CO 2 from CaCO 3 exited the reactor at CH 4 breakthrough. The experimental results have been validated with a pseudo homogeneous reactor model for the three reaction stages that *Manuscript Click here to view linked References