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Image Search Results
Journal: Membranes
Article Title: Synthesis and Characterization of 40 wt % Ce 0.9 Pr 0.1 O 2– δ –60 wt % Nd x Sr 1− x Fe 0.9 Cu 0.1 O 3− δ Dual-Phase Membranes for Efficient Oxygen Separation
doi: 10.3390/membranes10080183
Figure Lengend Snippet: Oxygen permeation fluxes through the Ce 0.9 Pr 0.1 O 2− δ –Nd x Sr 1− x Fe 0.9 Cu 0.1 O 3− δ ( x = 0.2, 0.5, 0.8) membranes (thickness: 0.6 mm) under air/He and air/CO 2 gradients at 1223 K.
Article Snippet: Test conditions: 150 mL min−1 synthetic air as the feed gas; 29 mL min −1 CO 2 as the sweep gas; 1 mL min −1 Ne as an internal standard gas; membrane thickness: 0.6 mm; Figure S3: XRD pattern of the sweep side (pure CO 2 ) of the Ce 0.9 Pr 0.1 O 2− δ –Nd 0.5 Sr 0.5 Fe 0.9 Cu 0.1 O 3− δ dual-phase membrane after 70 h O 2 permeation measurements as shown in Figure S2 under
Techniques:
Journal: Membranes
Article Title: Synthesis and Characterization of 40 wt % Ce 0.9 Pr 0.1 O 2– δ –60 wt % Nd x Sr 1− x Fe 0.9 Cu 0.1 O 3− δ Dual-Phase Membranes for Efficient Oxygen Separation
doi: 10.3390/membranes10080183
Figure Lengend Snippet: Long-term oxygen permeation flux through a Ce 0.9 Pr 0.1 O 2− δ –Nd 0.5 Sr 0.5 Fe 0.9 Cu 0.1 O 3− δ membrane at 1223 K under an air/He or air/CO 2 gradient. Test conditions: 0.65 mm membrane thickness; 150 mL min −1 synthetic air as the feed gas; 29 mL min −1 CO 2 as the sweep gas; 1 mL min −1 Ne as an internal standard gas.
Article Snippet: Test conditions: 150 mL min−1 synthetic air as the feed gas; 29 mL min −1 CO 2 as the sweep gas; 1 mL min −1 Ne as an internal standard gas; membrane thickness: 0.6 mm; Figure S3: XRD pattern of the sweep side (pure CO 2 ) of the Ce 0.9 Pr 0.1 O 2− δ –Nd 0.5 Sr 0.5 Fe 0.9 Cu 0.1 O 3− δ dual-phase membrane after 70 h O 2 permeation measurements as shown in Figure S2 under
Techniques: Membrane