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Review
. 2022 Jun 24;12(7):647.
doi: 10.3390/membranes12070647.

Dual-Phase Mixed Protonic-Electronic Conducting Hydrogen Separation Membranes: A Review

Affiliations
Review

Dual-Phase Mixed Protonic-Electronic Conducting Hydrogen Separation Membranes: A Review

Hongda Cheng. Membranes (Basel). .

Abstract

Owing to the excellent properties of high selectivity, high thermal stability, and low cost, in the past twenty years, mixed protonic-electronic conducting hydrogen separation membranes have received extensive attention. In particular, dual-phase mixed protonic-electronic conducting membranes with high ambipolar conductivity are more attractive because of the high hydrogen permeability. This paper aimed to present a review of research activities on the dual-phase membranes, in which the components, the characteristics, and the performances of different dual-phase membranes are introduced. The key issues that affect the membrane performance such as the elimination of the inter-phase reaction, the combination mode of the phases, the phase ratio, and the membrane configuration were discussed. The current problems and future trends were simply recommended.

Keywords: dual-phase; hydrogen separation; membrane; mixed protonic-electronic conducting.

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Conflict of interest statement

The authors declare no conflict of interest.

Figures

Figure 1
Figure 1
Schematic diagram of the bulk diffusion of protons through the membrane [17].
Figure 2
Figure 2
Schematic diagram of the transport of protons and electrons in dual-phase membranes.
Figure 3
Figure 3
Three Pd-based cermet dual-phase membranes with different hydrogen permeation fluxes [34].
Figure 4
Figure 4
The contribution of two diffusion mechanisms to the total hydrogen permeation fluxes in Ni-SCYb cermet dual-phase membranes [52].
Figure 5
Figure 5
H2 fluxes through Ni-BZCYb membrane feeding with dry and wet 4% H2 [41].
Figure 6
Figure 6
SEM images of Ni-BZCYYb sintered at 900 °C for 200 h in 20% CO2 containing atmosphere, (a) the original membrane, and (b) the sintered membrane [44].
Figure 7
Figure 7
XRD patterns of BCY-CYO after the stability test in atmosphere containing 4% H2 (B), H2O (C), 100% CO2 (D); original membrane (A) [66].
Figure 8
Figure 8
Hydrogen fluxes as a function of time for 60LWO-40LSC modified by La0.75Ce0.1Sr0.15CrO3-δ (LCeSC)-Ni feeding with different gases [77].
Figure 9
Figure 9
XRD of sintered cercer Y, cercer YYb, cercer YEu, and cercer YEr membranes. ■, perovskite phase; #, fluorite phase [65].
Figure 10
Figure 10
BaCe0.5Fe0.5O3-δ-based dual-phase membrane prepared by automatic phase separation technique [71].
Figure 11
Figure 11
The schematic diagram preparing independent distributed dual-phase membranes [74].
Figure 12
Figure 12
The schematic diagram of the phase distribution and the transport routs of protons and electrons, (a) dual-phase membrane prepared by simply powder blending, (b) laminated dual-phase membrane with short circuit pathways [74].
Figure 13
Figure 13
The preparation procedure of the asymmetric BCZY-GDC dual-phase membrane [69].

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