Ni-based oxygen carriers allow working at high temperatures (900-1100 degrees C) in a chemical-looping combustion (CLC) process with full CH4 conversion, although thermodynamic restrictions result in the presence of CO and H-2 in the gas outlet of the fuel reactor. On the other hand, Cu-based oxygen carriers allow complete fuel combustion to CO2 and H2O, but the operating temperature is limited due to the low melting point of the metallic Cu. The objective of this research was to analyze the behavior of several Ni-Cu oxygen carriers to reduce or avoid CO and H-2 emissions during a CLC process working at high temperatures. Commercial gamma-Al2O3 and alpha-Al2O3 were used as support to prepare by dry impregnation different oxygen carriers based on nickel and copper. The reactivity of these oxygen carriers was determined in a thermogravimetric analyzer (TGA). The effect of the mixture of NiO and CuO on the CO and H-2 generation was analyzed in a fixed bed reactor, and the gas product distribution during reduction/oxidation reactions was studied in a batch fluidized bed reactor working with CH4 as fuel and diluted air for oxidation. The fluidization behavior of the oxygen carriers with respect to the attrition and agglomeration processes was also analyzed during the multicycle batch fluidized bed tests. The presence of CuO in the Ni-Cu oxygen carriers allows the full conversion of CH4 to CO2 and H2O in the batch fluidized bed reactor during the initial part of the reduction time, and this time depended on the CuO content of the oxygen carrier. TGA and X-ray diffraction studies indicated that CuO is used for the reduction reaction before NiO. In addition, it was observed that the presence of NiO stabilized the CuO and allowed working at 950 degrees C with Ni-Cu oxygen carriers with a high metal oxide utilization.