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Cheng, H. Cermet and Cercer Dual-Phase Membrane. Encyclopedia. Available online: https://encyclopedia.pub/entry/25102 (accessed on 18 May 2024).
Cheng H. Cermet and Cercer Dual-Phase Membrane. Encyclopedia. Available at: https://encyclopedia.pub/entry/25102. Accessed May 18, 2024.
Cheng, Hongda. "Cermet and Cercer Dual-Phase Membrane" Encyclopedia, https://encyclopedia.pub/entry/25102 (accessed May 18, 2024).
Cheng, H. (2022, July 13). Cermet and Cercer Dual-Phase Membrane. In Encyclopedia. https://encyclopedia.pub/entry/25102
Cheng, Hongda. "Cermet and Cercer Dual-Phase Membrane." Encyclopedia. Web. 13 July, 2022.
Cermet and Cercer Dual-Phase Membrane
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This entry is adapted from the peer-reviewed paper 10.3390/membranes12070647

Based on different permeation mechanism, membrane for hydrogen separation can be categorized as mixed protonic–electronic conducting (MPEC) membrane, dense metal membrane, and porous inorganic membrane. Each membrane also has its own advantages and disadvantages. Cermet membrane is composed of a ceramic phase and a metal phase. The ceramic phase is benefit to improve the mechanical stability and high protonic conductivity of the membrane while the metal phase is used to enhance the electronic conductivity and surface-exchange kinetic. In order to overcome the drawbacks of cermet membranes, researchers developed another kind of dual-phase membrane (cercer membranes), in which a ceramic with high electronic conductivity replaces the metal as the electronic conducting phase.

dual-phase membrane mixed protonic-electronic conducting

1. Introduction

Over the past twenty years, with the development of the green economy, hydrogen has attracted considerable attention as one of the most important renewable and clean energy sources [1][2][3]. Each year the hydrogen consumption exceeds sixty million tons in industry [4]. To meet the rapidly increasing demand for hydrogen, many technologies have been developed to produce hydrogen, such as water electrolysis, methane steam reforming, and ammonia decomposition [5]. However, no matter what technology is used, hydrogen separation is one indispensable step because of the presence of by-products. At present, membrane technology, cryogenic distillation and swing adsorption (PSA) are the main hydrogen separation methods; among these, membrane technology is considered to be more promising owing to the advantages of ease of operation, cost efficiency, and process intensification opportunity [6][7][8]. Reactors based on hydrogen separation membrane can simultaneously carry out reaction and hydrogen purification in one unit, saving equipment space and capital costs [9][10].
Based on different permeation mechanism, membrane for hydrogen separation can be categorized as mixed protonic–electronic conducting (MPEC) membrane, dense metal membrane, and porous inorganic membrane. Each membrane also has its own advantages and disadvantages. Porous inorganic membranes such as zeolite membranes relay on molecular sieving mechanism, which possess high hydrogen permeability and good chemically stability. However, the low selectivity of hydrogen permeation restricts their application, especially on occasions when high purity hydrogen is required [11][12]. Palladium (Pd) or palladium alloy membranes possess excellent hydrogen permeation performance, but their large-scale commercial applications still are limited by the low thermal stability, poisoning by gas impurities, and the high cost [13][14][15][16]. As a notable membrane technique, MPEC membranes with high thermal stability and suitable price exhibit great development prospect in fields of hydrogen separation membranes, hydrogen sensors, and fuel cells [17]. Perovskite oxides Ba(Sr)CeO3 and lanthanide tungstate oxides LnWO (Ln = La, Nd, In, Sm) are the main materials prepared for MPEC membrane, and the hydrogen transport is achieved by the conduction of protons and electrons; moreover, the theoretical selectivity of hydrogen permeation can reach 100% [18][19][20][21]. Taking into account these advantages, MPEC membrane is of great promise as an applicative and economical hydrogen separation membrane.
Wanger and Shores first discovered that some metal oxides exhibited proton transport property when exposed to hydrogen at high temperatures, but the protonic conductivity was so poor that they did not attract much attention. After 1981, when Iwahara reported that some perovskite oxides exhibited obvious proton transport characteristics at high temperatures (≥600 °C), mixed protonic–electronic conducting membranes began to be intensively studied [22]. The hydrogen permeation of MPEC membranes begins with the combination of the hydrogen atom and the membrane intrinsic defects [23]; therefore, the concentration of intrinsic defects, especially the concentration of oxygen vacancy, is critical to the hydrogen permeability of MPEC membranes, more oxygen vacancy means higher protonic conductivity. To increase the oxygen vacancy of the membrane, and aliovalent doping is an effective approach. For ABO3 perovskite oxides, partially substituting B cations with aliovalent cations can efficiently increase the amount of oxygen vacancy. The doped perovskite oxides show obvious higher protonic conductivity compared with those of un-doped in hydrogen or water vapor containing atmosphere. Until now, a lot of trivalent cations including Y, Pr, Tb, Yb, and Sm have been used to substitute the cation of Ce or Zr in BaCe(Zr)O3 membranes [24][25][26]. The chemical stability, hydrogen permeation flux, and electrical conductivity of the doped membranes also have been thoroughly investigated. Similar to perovskite oxides, the doping strategy for lanthanide tungstate oxides are mainly focus on the partial substitution of W with Ir, Re, Mo, or Nb [27][28][29].
High ambipolar conductivity is necessary for MPEC membranes to gain high hydrogen permeation fluxes. Compared with the relatively high protonic conductivity, the lack of sufficient electronic conductivity restricts the practical application of MPEC membranes. The electronic conductivity of protonic conductor can be enhanced by aliovalent doping. It is found that the properties of the dopant ions such as the ionization potential is related to the membrane electronic conductivity [30]. For example, the electronic conductivity of SrCeO3-based membranes in reducing atmosphere increases with the increase of the dopant ion ionization potential [31]. However, the improvement of electronic conductivity by aliovalent doping is finite; moreover, this strategy could be detrimental to the protonic transport of the membrane. For example, while the p-type conductivity of Y-doped SrCeO3 is proportional to Y concentration, the protonic transport ability of the material declines following the increase of Y [32].
In recent years, dual-phase MPEC hydrogen separation membranes with high electronic and protonic conductivity have attracted great attention. The dual-phase MPEC membrane is fabricated by combing protonic conductor with an electronic conducting phase; in addition, according to the composition difference of the electronic conducting phase, dual-phase MPEC membranes are further divided into ceramic–metal (cermet) membranes and ceramic–ceramic (cercer) membranes, in which metal and ceramic with high electronic conductivity are used respectively.

2. Cermet Dual-Phase Membrane

Cermet membrane is composed of a ceramic phase and a metal phase. The ceramic phase is benefit to improve the mechanical stability and high protonic conductivity of the membrane while the metal phase is used to enhance the electronic conductivity and surface-exchange kinetic. Palladium (Pd) and nickel (Ni) are the common used metals in cermet membranes.

2.1. Pd-Based Cermet Membranes

Dense Pd membrane is a kind of membrane with excellent hydrogen permeability, and it can be applied to prepare high purity and high flux hydrogen. However, the low mechanical stability, low chemical stability, and the high cost restrict its industry application. In 2006, Argonne National Laboratory developed a cermet dual-phase membrane using Pd as the hydrogen transport metal and yttria-stabilized ZrO2 (YSZ) as the mechanically stable matrix [33]. The membrane showed a high hydrogen permeability, of which the H2 permeation rate reached 20 mL·min−1·cm−2 at 900 °C. Moreover, the membrane stability was investigated under H2S atmosphere. Hydrogen flux showed no degradation for 270 h in atmosphere containing 400 ppm H2S. The results indicated the combination of hydrogen separation metal and ceramic matrix can ensure the high hydrogen permeability and good mechanical stability of the membrane. Inspired by the excellent performance of Pd-YSZ, Jeon et al. fabricated a cermet dual-phase membrane by embedding Pd in protonic conducting ceramic matrix CaZr0.9Y0.1O3-δ (CZY) [34]. In this membrane, CZY is not only the matrix of Pd but also an active contributor for the hydrogen separation, facilitating the transport of protons through the membrane.

2.2. Ni-Based Cermet Membranes

Attributing to the unique properties, Ni is considered to be one of the most suitable metals used for conducting electrons in cermet membranes. As a well-known anode catalyst for fuel cells, Ni has high surface exchange kinetics, is cheaper, and has superior chemical and thermal stability compared with Pt. In addition, Ni has similar thermal expansion with BaCe0.9Y0.1O3-δ, which can enable Ni to have good compatibility with ceramic phases. Moreover, high sintering temperature is necessary to prepare a dense membrane, and the melting point of Ni is up to 1453 °C and can ensure the stability of the membrane during the sintering process.
The content of the metal phase in the composites is closely associated with the hydrogen permeability. To gain high hydrogen permeability, the amount of the metal phase needed in the composites should be firstly ascertained. Kim et al. studied the effect of membrane composition on the membrane electrical conductivity and hydrogen permeability [35]. The results showed that only when the Ni content reached 40 vol%, the metal phase could form a three-dimensional network and cause sufficient Ni connectivity. The membrane containing 40 vol% Ni had higher electrical conductivity and H2 permeability compared with the membranes with 30 and 35 vol% Ni. As shown in Table 1, Ni content in most of the current Ni-based dual-phase membranes was set to 40 vol%. Song et al. prepared cermet composite Ni-SrCe0.8Yb0.2O3-x (Ni-SCYb) containing 40 vol% Ni via ball-milling method. Both the membrane electronic conductivity and surface exchange kinetics were improved distinctly. The hydrogen flux was ten times that of single SCYb membrane. Hydrogen permeation due to the atomic diffusion through Ni phase was also detected (Figure 1). However, compared with Pd-based composite membranes, the atomic hydrogen diffusion of Ni is much weaker, and the ambipolar diffusion of SCYb was dominant over the whole temperature range [36].
Table 1. Cermet membranes with different hydrogen permeation performances.
Composition Hydrogen Flux
(mL·min−1·cm−2)		 T (°C) Thickness
(mm)		 Feed/Sweep Gas Note Ref.
50Pd-50YSZ 20 900 0.22 100%H2/N2 mechanical mixing [33]
50Pd-50YSZ 5.5 900 0.218 80% H2-He/N2 ball-milling [37]
50Pd-50YSZ 52 900 0.018 100%H2/N2 mechanical mixing; asymmetric [38]
50Pd-50Gd0.2Ce0.8O2-δ 5.5 900 0.282 80% H2-He/N2 ball-milling [39]
50Pd-50CaZr0.9Y0.1O3-δ 2.3 900 0.50 80% H2-He/N2 ball-milling [34]
50Pd-50BaCe0.4Zr0.4Gd0.1Dy0.1O3-δ 2.77 700 0.40 100%H2/N2 ball-milling [40]
40Ni-60BaZr0.7Pr0.1Y0.2O3-δ 0.0162 950 0.40 wet50%H2-N2/Ar mechanical mixing [41]
50Ni-50BaCe0.85Te0.05 Zr0.1O3-δ 0.17 800 0.50 50%H2-He/Ar mechanical mixing [42]
40Ni-60BaZr0.1Ce0.7Y0.2O3-δ 0.805 900 0.266 100%H2/N2 ball-milling [43]
40Ni-60BaZr0.1Ce0.7Y0.2O3-δ 0.056 900 1 100%H2/N2 ball-milling [44]
40Ni-60BaZr0.1Ce0.7Y0.2O3-δ 0.087 900 0.5 wet4%H2-Ar/N2 ball-milling [45]
40Ni-60BaZr0.1Ce0.7Y0.1Yb0.1O3-δ 0.0174 900 0.75 20%H2-He/N2 mechanical mixing [46]
40Ni-60BaZr0.1Ce0.7Y0.1Yb0.1O3-δ 0.215 900 0.40 wet80%H2-He/N2 mechanical mixing [47]
50Ni-50BaCe0.95Tb0.05O3-δ 0.53 850 0.65 50%H2-He/N2 ball-milling [48]
50Ni-50BaCe0.95Tb0.05O3-δ 0.914 850 0.09 50%H2-He/N2 ball-milling; asymmetric [48]
40Ni-60BaCe0.9Y0.1O3-δ 0.24 900 0.08 wet3.8%H2-He/N2 ball-milling [49]
40Ni-60BaCe0.9Y0.1O3-δ 0.76 800 0.23 100%H2/N2 high-energy milling [35]
50Ni-50BaCe0.85Fe0.15O3-δ 0.325 1000 0.50 50%H2-He/wet Ar ball-milling [50]
40Ni-60BaCe0.7In0.2Ta0.1O3-δ 0.15 900 1 20%H2-N2/Ar mechanical mixing [51]
40Ni-60BaCe0.7Y0.2In0.1O3-δ 0.013 850 0.86 20%H2-N2 /Ar mechanical mixing [52]
40Ni-60SrCe0.8Yb0.2O3-δ 0.105 900 0.25 wet20%H2-He/N2 ball-milling [36]
40Ni-60La0.5Ce0.5O2-δ 0.088 900 0.048 20%H2-N2/Ar mechanical mixing; asymmetric [53]
40Ni-60La0.5Ce0.5O2-δ 0.021 900 0.6 wet20%H2-N2/Ar ball-milling [54]
40Ni-60La0.4875Ca0.0125Ce0.5O2-δ 0.025 900 0.6 wet20%H2-N2/Ar ball-milling [54]
40Ni-60La1.95Sm0.05Ce2O7 0.037 900 0.6 wet20%H2- Ar/N2 ball-milling [55]
60Ni-40La5.5WO11.25-δ 0.18 1000 0.5 50%H2-He/Ar ball-milling [56]
Cu-BaZr0.9Y0.1O3-δ 0.00242 882 1.90 100%H2/Ar molten-copper infiltration
technique		 [57]
60Ta-40YSZ 1.2 500 0.50 100%H2/Ar mechanical mixing [58]
Figure 1. The contribution of two diffusion mechanisms to the total hydrogen permeation fluxes in Ni-SCYb cermet dual-phase membranes [36].
Since the electronic conductivity of the Ni phase decreases at elevated temperatures, enhancement of membrane permeability at high temperatures should be attributed to the improvement of the protonic conductivity of the ceramic phase. Therefore, for Ni-based dual-phase membranes, the hydrogen permeability mainly depends on the protonic conductivity of the ceramic phases. For the Ni phase, although the electronic conductivity decreases at high temperatures, the hydrogen permeability increases because of the improvement of the atomic diffusion.
The stability is important for hydrogen separation membranes, especially for dual-phase membranes under vapor or CO2-containing atmosphere. Humidity is favorable for the ceramic phase; both the catalytic activity and protonic conductivity of the ceramic phase will be enhanced owning to the hydration of the membrane. However, humidity is unfavorable for the metal phase; the conductivity of the metal phase will decrease in wet atmosphere due to the oxidizing of the surface. Zuo et al. studied the hydrogen permeability of Ni-Ba(Zr0.8-xCexYb0.2)O3-α (Ni-BZCYb) membrane under wet conditions. As shown in Figure 2, Ni-BZCYb had higher hydrogen fluxes under wet conditions [43]. The stability of composite membrane Ni-BaZr0.1Ce0.7Y0.1Yb0.1O3-δ (Ni-BZCYYb) was tested under wet CO2 atmosphere. The hydrogen flux kept stable in wet 30 vol% CO2. As shown in Figure 3, no microstructure change happened on the membrane surface after the stability test. The researchers attributed the excellent performance of the membrane to the Zr, Yb co-doping, and the modified membrane preparation method [47].
Figure 2. H2 fluxes through Ni-BZCYb membrane feeding with dry and wet 4% H2 [43].
Figure 3. 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 [46].

3. Cercer Dual-Phase Membrane

Owing to the combination of a metal phase and a ceramic protonic conductor, the mixed protonic-electronic conductivity of cermet dual-phase membranes is significantly improved compared with ceramic single-phase membranes. However, cermet membranes still exhibit some unresolved issues, such as the oxidation of the metal phase under high temperatures and the thermal expansion coefficient mismatch between metal and ceramic. In order to overcome the drawbacks of cermet membranes, researchers developed another kind of dual-phase membrane (cercer membranes), in which a ceramic with high electronic conductivity replaces the metal as the electronic conducting phase. Because both the electronic and protonic conducting phases of the membrane are ceramic, the chemical and thermal property compatibility of the membrane can be effectively improved. Unemoto first proposed the concept of cercer dual-phase membrane and investigated the electronic conductivity and hydrogen permeation properties of a model membrane, SrZrO3-SrFeO3 [59].

3.1. Barium Cerate-Based Cercer Membranes

As one of the advanced hydrogen-permeation materials, doped BaCeO3 is the most commonly used protonic conducting phase in cercer membranes and has the highest protonic conductivity among the oxide protonic conductors. In addition, it also presents a nonnegligible electronic conductivity especially at high temperatures, and its electronic conductivity is the highest among the perovskite protonic conductors [48][60]. So far, the main electronic conducting phases used for barium cerate cercer membranes include fluorite oxides Y, Gd- or Sm-doped CeO2, Nb-doped SrTiO3, and SrFeO3.
Rosensteel et al. designed a type of cercer hydrogen separation membrane using Y-doped BaCeO3 (BCY) and CeO2 (CYO) as the protonic and electronic conducting phase respectively. Fully dense dual-phase membranes were prepared via a single synthesis and sintering step. As a good electron conductor, CYO largely enhanced the membrane electronic conductivity [61]. Ivanova et al. also reported a cercer membrane BaCe0.8Eu0.2O3-δ-Ce0.8Y0.2O2-δ (BCEO-CYO), which exhibited a remarkable high hydrogen permeation flux up to 0.61 mL·min−1·cm−2 at 700 °C. It was observed that Eu had a strong tendency to migrate from the BCEO phase to CYO phase, leading to a significant Eu-depleted BCEO [62]. The electronic conductivity of three kinds of electronic conducting phases at 800 °C follows the trend of Sr0.95Ti0.9Nb0.1O3-δ (200 S·cm−1) > Sm0.8Y0.2O2-δ (0.39 S·cm−1) > Ce0.8Y0.2O2-δ (0.35 S·cm−1) [63][64][65].
The protonic conductivity of doped BaCeO3 is excellent. Theoretically, its chemical stability should be poor under CO2 atmosphere because there is a reaction between BaCeO3 and CO2 at high temperatures. However, as shown in the XRD images of BCY-CYO after the stability tests (Figure 4), compared with BaCeO3 single-phase membranes, the carbonate compounds generated reduced greatly under CO2 atmosphere, and as a result, the chemical stability of the membrane was significantly improved. Liu et al. further speculated the improvement of chemical stability attributed to the formation of CeO2; CeO2 inhibited the reaction between CO2 and BaCeO3. As shown in Equation, the presence of CeO2 makes the reaction proceed to the direction of forming BaCeO3, thus protecting the perovskite structure [66].
BaCe 0.8 Y 0.2 O 3 + CO 2 ⇌ BaCO 3 + 0.8 CeO 2 + 0.1 Y 2 O 3
Figure 4. XRD patterns of BCY-CYO after the stability test in atmosphere containing 4% H2 (B), H2O (C), 100% CO2 (D); original membrane (A) [66].

3.2. Lanthanum Tungstate Cercer Membranes

Lanthanide tungstate oxides (LnWO, Ln = La, Nd, In, Sm) are important potential candidates used for hydrogen-separation membranes. These compounds present single defective fluorite structures while the ratio of Ln/W is in the range of 5.3 to 5.7. Besides the good protonic conductivity, lanthanide tungstate oxides exhibit better chemical stability against H2O, CO2, and H2S than perovskite materials. Lanthanum tungstate (LWO) is one of the main lanthanide tungstate oxides; this material has significant hydrogen permeability at temperatures above 800 °C, but with insufficient permeability at temperatures less than 700 °C because of the low electronic conductivity. Escolástico et al. prepared a La5.5WO11.25-δ-La0.87Sr0.13CrO3-δ (LWO-LSC) dual-phase membrane using LSC, in which LSC, used as the electronic conductivity phase, had both high p-type electronic conductivity and remarkable stability in reducing atmosphere. The dense membrane was obtained by sintering at 1400 °C and the H2 flux at 700 °C reached 0.15 mL·min−1·cm−2, exhibiting a higher permeability than most of the BaCeO3-based cercer membranes [67]. The combination of LWO and LSC solved the abovementioned problem of LWO single-phase membranes well. Besides these, the stability and proton transport of composite membrane LWO-LSC was investigated under CH4 atmosphere. Hydrogen flux remained unchanged for 5 h when 30% CH4 was contained in the feed gas (Figure 5). The membrane stability under high steam content methane was also evaluated. After annealing at 700 °C and 3 bars for 24 h in 50% CH4-H2O atmosphere, the membranes kept totally dense and no secondary phase was found [68].
Figure 5. Hydrogen fluxes as a function of time for 60LWO-40LSC modified by La0.75Ce0.1Sr0.15CrO3-δ (LCeSC)-Ni feeding with different gases [68].

3.3. Elimination of the Inter-Phase Reaction

To obtain a dense membrane, a high-temperature sintering process is inevitable for the preparation of composite membranes. However, high temperatures tend to cause inter-phase reactions inside the membrane, generating undesirable phases which may damage the performances of the membrane. Adding sintering aid is an efficient method to decrease the sintering temperature, and then decrease the inter-phase reaction. Rebollo prepared BaCe0.65Zr0.20Y0.15O3-δ-Ce0.83Gd0.15O2-δ dual-phase membrane via a single synthesis and sintering step using ZnO as the sintering aid. Dense membranes without any cracks were obtained by sintering treatments at 1450 °C. The addition of the sintering aid decreases the sintering temperature and avoids the detrimental of high temperature to the membrane mechanical and electrical properties [69]. Meng et al. fabricated a dual-phase membrane using ZnO and SrCe0.95Y0.05O3-δ. ZnO was used as both sintering aid and electronic conductor in the membrane. The membrane was sintered at 1200 °C and there was no new phase formed during the sintering progress. The membrane possessed the highest conductivity when the content of ZnO reached 20 wt% [70]. Wang et al. synthesized Zn doped BaZr0.9Y0.1O3-δ-BaCe0.86Y0.1Zn0.04O3-δ dual-phase membranes by gel polymerization method; attributed to the doping of Zn, the membranes were well-sintered at 1350 °C and no extra phase was generated. In contrast, the non-doped membranes still kept their porous structure even when sintered at 1500 °C [71]. Updating sintering technologies also is one of the important methods to decrease the sintering temperature and eliminate the inter-phase reaction.

3.4. Phase Composition Ratio

For cercer dual-phase membrane, both high protonic and electronic conductivity are necessary to obtain high hydrogen permeability, yet the phase ratio of the membranes have a great influence on the protonic and electronic conductivity. Therefore, to ensure high and comparable protonic and electronic conducting ability, the phase ratio of the membranes should be carefully investigated.
Escolástico et al. prepared different composite membranes using La5.5WO11.25-δ (LWO) and La0.87Sr0.13CrO3-δ (LSC); the phase ratio was set as 2/8, 3/7, 4/6, and 7/3 respectively. The results showed that the 20%LWO-LSC composite had the highest total conductivity while the 50%LWO-LSC composite exhibited the highest hydrogen permeability [67]. Polfus et al. prepared La27W3.5Mo1.5O55.5-δ-La0.87Sr0.13CrO3-δ (LWMO-LSC) cercer composite membranes with different phase ratios. The results showed that the best permeability was obtained by the membrane of 70LWMO-30LSC in which complete electronically conducting phase percolation might not be formed [72]. Similar to LWMO-LSC membrane, BCY-CYO membrane with phase ratio of 3/7 possessed the highest total conductivity and highest hydrogen permeability [66]. It indicates that the electronic or protonic conducting phase in composite membrane may not be necessary to form a continuous network, which has ever been considered needed for high hydrogen permeability. Adding too much electronic conducting phase not only has no benefit to the hydrogen permeability but also can choke off the conductivity of the protonic conducting phase. The hydrogen permeability enhancement should be attributed to the effective combination of the protonic and electronic phases, which brings about high ambipolar conductivity.

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Hongda Cheng
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