Co-free La0.9Ca0.1Fe1-xCuxO3-δ (x = 0.05, 0.1) hollow fiber membranes for H2/N2 and H2/CO co-production by coupling water splitting and partial oxidation of methane

Mixed ionic-electronic conducting oxygen transport membranes have demonstrated high oxygen permeability, which can be coupled with other oxidation reactions. The membrane reactor coupling water splitting with partial oxidation of methane (CH 4 ) reaction has great practical potential as it produces valuable feedstocks such as ammonia syngas and liquid fuel syngas. However, the existing membrane materials often exhibit structural stability issue and/or unsatisfactory oxygen permeability. In this work, Cu-doped LCF 1-x Cu x O 3-δ (x = 0.05-0.1) hollow fiber membranes were used for hydrogen (H 2 ) production by coupling the oxygen separation with water splitting and partial oxidation of methane. A small amount of Cu doping could effectively reduce the sintering temperature of the membrane and increase the conductivity of the material, where a maximum oxygen flux of 0.55 mL min -1 cm -2 was achieved on LCFCu 0.05 membrane under the experimental conditions. In the water splitting test, a maximum H 2 production rate of 3.7 mL min -1 cm -2 was achieved by using steam as the raw gas (driven by nitrogen) at the shell side and H 2 /helium (He) mixture as the sweep gas at the lumen side of the LCFCu 0.05 hollow fiber membrane with 10 wt.% Ni/SDC on the shell side. As pure CH 4 gas was introduced at the lumen side coated with Ni/LaNiO 3 /γ-Al 2 O 3 catalyst, the H 2 production rate was further increased to its highest of 4.4 mL min -1 cm -2 . In addition, the membrane reactor could be stably operated for 300 hours under three different flow conditions without performance degradation. These results paves the development of robust membrane reactor for integrated water splitting and partial oxidation of methane. • New Cu-doped La 0.9 Ca 0.1 Fe 0.95 Cu 0.05 O 3-δ (LCFC) hollow fibre membrane. • LCFC demonstrated high O 2 flux of 0.55 mL min -1 cm -2 at 950 o C with He sweep gas. • Coupled water splitting and partial oxidation of methane for more than 310 hours. • Co-production of H 2 /N 2 and H 2 /CO syngas through the coupled reactions. • The achieved H 2 flux was 3.7 mL min -1 cm -2 with catalyst.