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Article

Synthesis and Characterization of 40 wt % Ce0.9Pr0.1O2–δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δ Dual-Phase Membranes for Efficient Oxygen Separation

by
Guoxing Chen
1,*,
Zhijun Zhao
2,
Marc Widenmeyer
1,
Ruijuan Yan
1,
Ling Wang
1,
Armin Feldhoff
2 and
Anke Weidenkaff
1,3,*
1
Department of Materials and Earth Sciences, Technische Universität Darmstadt, Alarich-Weiss-Str. 2, 64287 Darmstadt, Germany
2
Institute of Physical Chemistry and Electrochemistry, Leibniz University Hannover, Callinstr. 3A, 30167 Hannover, Germany
3
Fraunhofer Research Institution for Materials Recycling and Resource Strategies IWKS, Brentanostraße 2a, 63755 Alzenau, Germany
*
Authors to whom correspondence should be addressed.
Membranes 2020, 10(8), 183; https://doi.org/10.3390/membranes10080183
Received: 27 July 2020 / Accepted: 10 August 2020 / Published: 12 August 2020
(This article belongs to the Special Issue Oxygen Transport Membranes: Synthesis and Applications)
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Abstract

:
Dense, H2- and CO2-resistant, oxygen-permeable 40 wt % Ce0.9Pr0.1O2–δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δdual-phase membranes were prepared in a one-pot process. These Nd-containing dual-phase membranes have up to 60% lower material costs than many classically used dual-phase materials. The Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ sample demonstrates outstanding activity and a regenerative ability in the presence of different atmospheres, especially in a reducing atmosphere and pure CO2 atmosphere in comparison with all investigated samples. The oxygen permeation fluxes across a Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane reached up to 1.02 mL min−1 cm−2 and 0.63 mL min−1 cm−2 under an air/He and air/CO2 gradient at T = 1223 K, respectively. In addition, a Ce0.9Pr0.1O2–δ–Nd0.5Sr0.5Fe0.9Cu0.1O3–δ membrane (0.65 mm thickness) shows excellent long-term self-healing stability for 125 h. The repeated membrane fabrication delivered oxygen permeation fluxes had a deviation of less than 5%. These results indicate that this highly renewable dual-phase membrane is a potential candidate for long lifetime, high temperature gas separation applications and coupled reaction–separation processes.

Graphical Abstract

1. Introduction

The change from a fossil fuel-based to a renewable energy-based system requires the development of resource efficient materials with a long lifetime for energy conversion technologies. In this regard, mixed ionic–electronic conducting (MIEC) oxygen transport materials have drawn increasing interest due to their high potential for various energy conversion applications such as the oxygen transport membrane (OTM) for producing oxygen from air [1,2,3,4,5,6,7,8,9,10,11,12], electrolytes for batteries [13,14,15], cathode materials for solid oxide fuel cells [16,17,18], catalysts [19,20,21], and in membrane reactors [21,22,23]. With the current background of increases in CO2 emissions and fossil resources depletion, CO2 capture and utilization have been intensively researched to reduce CO2 emissions, including thermolysis, photocatalysis, plasma, and electrochemical methods [24]. OTMs, processed in integrated oxy-fuel combustions, provide the oxygen supply and have been considered to be a highly efficient and cost-effective way of capturing CO2. Using the OTMs membrane technology, the costs and energy consumption for oxygen production could be reduced at least by 35% compared with the conventional cryogenic distillation method [25,26]. Besides the application of the separation of oxygen from air, MIEC membranes used in membrane reactors are getting increasing attention to couple the reaction and separation processes to save energy and simplify the process [21,22,23,27,28]. Plasma technologies have attracted increasing attention as a timely flexible method for CO2 conversion and utilization [29,30,31,32,33]. For example, plasma-assisted MIEC membranes, used to separate oxygen radicals without additional external heating from the decomposition products, provide an efficient way to enhance the overall CO2 conversion efficiency via inhibiting the reverse reactions [27,28]. Traditional OTMs, which have been intensively investigated in recent years, are usually Ba2+- or Sr2+-containing perovskite-type oxides, such as Ba1−xSrxCo1−yFeyO3−δ, which show excellent oxygen permeabilities [4,5,34,35,36,37,38,39]. However, due to their vulnerability in CO2-containing environments, the widespread industrial applicability is strongly limited [1,4]. Although many studies have been devoted to modify perovskite-type OTMs to improve CO2 resistance with an appropriate selection of A- and B-site cations [40,41,42,43,44,45], most of such perovskite-type membranes are still susceptible to the formation of carbonates in the presence of CO2 due to unfavorable thermodynamics [15].
Dual-phase membranes consisting of mechanically and chemically robust fluorite oxides as an oxygen ionic conducting phase and a Ruddlesden–Popper, perovskite, or spinel oxide as an electronic conducting phase, are promising alternatives to ensure chemical and mechanical stability and a high oxygen permeability. For choosing the ionic conducting materials, three criteria should be fulfilled as discussed by Zhu et al. [2]: (i) high ionic conductivity; (ii) high chemical resistance under reducing or acidic (such as CO2) gas atmospheres; (iii) good chemical compatibility with the selected electronic conducting materials. Ceria-based materials with a fluorite structure fulfil these three criteria and have been well-established as ionic conductor phases for oxide anions in dual-phase membranes. Besides, the formation of continuous ionic and electronic conducting paths in dual-phase membranes is needed. To ensure this, MIEC oxides (such as LnxSr1−xFeO3−δ Ln = lanthanides) providing both electronic and oxygen ionic transport paths are often considered as promising electronic conducting materials [2,3,4,6,46,47,48,49,50,51,52]. Similar selection criteria for the ionic conducting material have to be considered allowing for high electronic conductivity in combination with a high chemical and thermal compatibility [4]. The above-mentioned factors have made Ce0.8Sm0.2O2−δ–Sm0.5Sr0.5Fe0.8Cu0.2O3−δ (CSO-SSFCO), Ce0.9Pr0.1O2−δ–Pr0.6Ca0.4FeO3−δ (CPO-PCFO), Ce0.8Gd0.2O2−δ–Pr0.5Sr0.5Fe0.5Co0.5O3−δ (CGO-PSFCO), and Ce0.9Nd0.1O2−δ–Nd0.6Sr0.4CoO3−δ (CNO-NSCO) intensively investigated materials [2,3,4,6,46,47,48,49,50,51,52,53,54,55,56,57,58,59,60,61,62,63,64,65,66,67]. Although the CO2 resistance has been improved, most of their oxygen permeation fluxes are still too low to meet the requirements for practical applications. Therefore, OTMs which combine good chemical stability in different varying atmospheres with a high oxygen permeability are still highly needed for long lifetime industrial applications. Omar et al. found that Nd-doped ceria exhibits the highest ionic conductivity among 10 mol% rare earth (Gd, Er, Lu, Dy, Yb, Y, Sm, Sm/Nd, Nd)-doped ceria systems prepared under similar conditions [68]. Based on these findings, a Nd-containing dual-phase membrane with the composition 60 wt % Ce0.9Nd0.1O2−δ–40 wt % Nd0.6Sr0.4FeO3−δ has been developed by Luo et al. [49]. A high oxygen permeation flux of 0.48 mL min−1 cm−2 was obtained for the membrane (0.6 mm thickness) with a porous La0.6Sr0.4CoO3−δ coating layer using CO2 as sweep gas at 1123 K. In a recent study, the same authors designed and synthesized another novel Nd-containing dual-phase membrane (Ce0.9Nd0.1O2−δ–Nd0.6Sr0.4CoO3−δ), and the oxygen permeation flux was improved to 0.55 mL min−1 cm−2 through a membrane (0.6 mm thickness) under an air/CO2 gradient at 1223 K [50]. However, the oxygen permeation flux is still lower than other reported dual-phase membranes but still competitive in particular if the up to 60% lower materials cost are considered. In addition, the reproducibility and level of regeneration of the dual-phase membranes have received less attention in the literature for the oxygen transport process. In our previous studies on dual-phase membranes, different Ce0.9Pr0.1O2−δ:La0.5Sr0.5Fe0.9Cu0.1O3−δ weight ratios (20%:80%, 40%:60%, 60%:40%, and 80%:20%,) were presented, with the highest permeation fluxes under an air/He and an air/CO2 gradient found for a weight ratio of 40%:60% [6]. Thus, inspired by the reported studies and our previous studies [6,49,50,68], here we report the CO2-resistant dual-phase 40 wt % Ce0.9Pr0.1O2−δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) membranes prepared by a one-pot synthesis. This approach offers the possibility to upscale the production by a continuous spray combustion aerosol process for industrial applications [69]. The desired structural and compositional stability or level of regeneration and the simultaneous continuous oxygen permeability under air/CO2 and air/He gradients of these dual-phase membranes are investigated in view of an enhanced lifetime for a robust active system. The dual-phase membranes are tested towards CO2 at different temperatures and times in order to study the chemical resistance under a CO2 atmosphere. Long-term CO2 stability and oxygen permeability are monitored and evaluated. In addition, the reproducibility and level of regeneration of the dual-phase membranes have been confirmed for a power-to-x conversion application.

2. Experimental

2.1. Preparation of Powders and Membranes

CO2-tolerant 40 wt % Ce0.9Pr0.1O2−δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) dual-phase membranes were prepared by the same one-pot method as previously reported for Ce0.9Pr0.1O2−δ–La0.5Sr0.5Fe0.9Cu0.1O3−δ [6] using Nd(NO3)3·6H2O (99.9%, Alfa Aesar, Kandel, Germany) instead of La(NO3)3·6H2O. Then, the as-prepared Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ dual-phase powders were pressed with 60 kN (equals 40 MPa for a 16 mm diameter) to get the green disks. These green disks were sintered at 1323 K for 15 h in air (3 K min−1 heating and cooling rate). The desired membrane thickness (~0.6 mm) was adjusted by polishing with a 600 grit sandpaper. The thickness of the membranes used for oxygen permeation tests were 0.6 - 0.65 mm.

2.2. Materials Characterization

Powder X-ray diffraction (XRD, Mo-Kα1, a STOE STADI P X-ray diffractometer, Darmstadt, Germany) was used to identify the phase structures of the samples at room temperature. In situ XRD measurements were performed from 303 K to 1123 K in air (Bruker D8 Advance instrument with Mo-Kα1 radiation, Billerica, MA, USA). Thermogravimetric analysis (TGA) measurements were performed to characterize the weight changes of the as-prepared membranes (NETZSCH STA 449C, Selb, Germany) in different atmospheres (pure CO2, air, Ar or 5% H2-95% Ar). The powder samples were placed in a NETZSCH STA 449F3 (Selb, Germany) for various times and temperatures in order to investigate the chemical stability towards CO2. Scanning electron microscopy (SEM, Zeiss Gemini 500, Oberkochen, Germany) was used to study the microstructures of the prepared dual-phase membranes. The elemental distributions were investigated by energy-dispersive X-ray spectroscopy (EDXS) (Bruker XFlash 6|60, Billerica, MA, USA).

2.3. Oxygen Permeation Measurements

Oxygen permeability measurements were carried out on a home-made high-temperature permeation device shown in Figure S1. The disk membranes were sealed on an alumina tube (16 mm) with a gold paste (CHEMPUR, Karlsruhe, Germany). In this work, synthetic air was used as the feed gas and CO2 or He as the sweep gas. A detailed description of the setup and process parameters for oxygen permeation measurements can be found in our previous studies [6,40]. Concerning the oxygen permeation tests, four different 40 wt % Ce0.9Pr0.1O2−δ–60 wt % Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membranes have been tested to investigate the reproducibility and level of regeneration. Partly due to the leakage of the gold sealing paste, a higher nitrogen concentration in the permeate gas was detected. The purity of the permeating O2 is around 65%~85% for different oxygen permeation tests. All oxygen permeation measurements were leakage corrected.

3. Results and Discussion

3.1. Structure Characterization and Morphologies

The XRD patterns of the Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) powders and the reference samples (Ce0.9Pr0.1O2−δ and NdxSr1–xFe0.9Cu0.1O3−δ) are shown in Figure 1. Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ and Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ composite materials are composed of a fluorite-type phase and a perovskite-type phase, indicating a sufficient chemical compatibility between Ce0.9Pr0.1O2−δ and NdxSr1–xFe0.9Cu0.1O3−δ(x = 0.2 and x = 0.5). However, with a further increasing Nd content (x = 0.8), an additional weak reflection at 2θ = 11.8° points to the presence of an unidentified impurity phase, which suggests some reaction occurring, thus, a reduced chemical compatibility between Ce0.9Pr0.1O2−δ and Nd0.8Sr0.2Fe0.9Cu0.1O3−δ.
SEM-EDXS analyses were conducted to investigate the feasibility of the dual-phase membranes. Figure 2 displays the SEM and EDXS micrographs of fresh Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ dual-phase membranes. The grains are closely packed without cracks for Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ and Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ samples. Ce0.9Pr0.1O2−δ and NdxSr1–xFe0.9Cu0.1O3−δ grains can be clearly distinguished, as shown in Figure 2a,b, which indicates a good chemical compatibility of the two phases in the dual-phase membranes. The Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ sample reveals a smaller average grain diameter than Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ and Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ samples. In addition, small amounts of pinholes are found as shown in Figure 2c. These observations demonstrate that a suitable Nd content in the dual-phase membranes can form a good percolation network with well-separated oxygen ion conductor (Ce0.9Pr0.1O2−δ) and mixed ionic electronic conductor (NdxSr1–xFe0.9Cu0.1O3−δ).

3.2. Materials Tolerance towards Air, CO2 and H2

The TGA curves of Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) dual-phase membranes under air, CO2, Ar, and 5 vol% H2-95 vol% Ar atmospheres are shown in Figure 3, in order to determine the potential carbonate formation, CO2 adsorption ability, oxygen vacancy formation, as well as H2 tolerance of the membranes. The TGA curves of membrane materials reveal a comparable response to the changes of the gas atmosphere. The higher the reductive power (air < CO2 < Ar < Ar/H2) of the surrounding gas atmosphere, the larger the resulting mass change. A second general trend is that the higher the Sr content in Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) the easier, meaning it can be obtained at a lower temperature, and the stronger the occurring mass change. A similar trend of an increasing mass change has been reported in other studies for perovskite-type samples with higher contents of Sr2+ [36,70]. In contrast to Ar/H2 atmospheres, Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ revealed a more or less continuous mass change upon heating to 1473 K in air, CO2 and Ar. This points to a formation of oxygen vacancies by local thermal reduction. An exception is Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ since it shows a reversible mass change above 1000 K under CO2 exposure. This can be attributed to the higher Sr content and enlarged sensitivity towards the intermediate formation of SrCO3. As a result of the stronger CO2 adsorption ability of Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ, a smaller mass change is measured. For Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.5, 0.8), no indications of carbonate formation were visible. The very similar measurement values of the total mass changes at 1473 K as in Ar may suggest a certain adsorption of CO2 on the membrane surface and have to be further investigated (see below). A similar behavior was already reported in our previous study [40]. In the Ar/H2 atmosphere, a clearly different progression of the TGA curves was observed. In the temperature range 600 K ≤ T ≤ 800 K, a defined mass change was obtained resulting from a change in the perovskite phase. However, the exact origin is still unknown. This is around 900 K followed by a continuous mass change pointing again to a thermal reduction by oxygen vacancy formation. Another obvious feature of the TGA curves is that Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ showed the easiest reaction in the first step, while the thermal reduction at a higher temperature follows the trend as observed in the other gas atmospheres. This can be explained by the determined differences in the microstructure of the membrane materials, since Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ has a much smaller grain size (Figure 2) resulting in an easier access of H2 from the surrounding gas atmosphere. Figure 4 shows the XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) samples after TGA measurements under a CO2 atmosphere. Evidently, no secondary phases and carbonates are found for Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ, while some additional unidentified impurity phases causing reflections at about 2θ = 11.5°, 21.2°, and 24° are formed for Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ and Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ samples. These results point to a good thermal and chemical compatibility under a CO2 atmosphere and can be achieved with a suitable Nd content in the dual-phase membranes.
Figure 5 shows the XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) bulk samples before and after TGA measurements under a 5 vol% H2-95 vol% Ar atmosphere (Figure 3d). Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ almost maintained its structure with the formation of a small fraction of unidentified impurity phases, while Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ and Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ were heavily destroyed by large fractions of impurity phases. This demonstrates that Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ has the largest resistance against reducing conditions.
To study the phase stability of the membrane materials, Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) powders were evaluated by in situ XRD measurements in air. As displayed in Figure 6a, some additional reflections appear when the temperature goes up to 1123 K and still can be observed even after cooling down to 873 K for sample Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ. Similarly, for sample Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ (Figure 6c), some unidentified impurity phases were formed when the temperature goes up to 1073 K and still can be found even after cooling down to 873 K. Interestingly, as shown in Figure 6b for sample Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ, no structural phase transition and additional reflections were observed in the whole temperature range during heating and cooling in air. Both the perovskite-type phase and the fluorite-type phase remain unchanged. Thermal expansion coefficients of Ce0.9Pr0.1O2−δ and Nd0.5Sr0.5Fe0.9Cu0.1O3−δ are 7.27(3) × 10−5 K−1 and 5.30(5) × 10−5 K−1, respectively, in the temperature range 295–1123 K based on the XRD patterns in Figure 6b. All these results indicate a good chemical compatibility of these two phases and good structural stability in air.
In order to further study the CO2 tolerance of Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) membrane materials, several groups of experiments in the presence of CO2 were carried out and the results were given in Figure 7. Figure 7a shows the XRD patterns of all the samples after an exposure to CO2 at 1173 K for 100 h. It can be seen that no formation of carbonates and impurity phases happened for all the Nd-containing dual-phase samples. To gain a more accurate conclusion on the CO2 tolerance of Nd-containing dual-phase materials, Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ powder samples were treated in the presence of CO2 at different temperatures for 2 hours (773~1173 K) and the XRD patterns were displayed in Figure 7b. No formation of carbonates was found for the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ samples at any temperatures comparing the XRD patterns of the pristine samples, which indicates a high chemical and thermal stability when in CO2 atmospheres. In addition, extending the exposing time to 100 h and 500 h as shown in Figure 7c, the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ sample still kept its original structure.

3.3. Oxygen Permeation Measurements

The oxygen permeation fluxes of the Ce0.9Pr0.1O2–δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) membrane disks with a 0.6 mm thickness were measured at 1223 K under air/He and air/CO2 gradients. The oxygen permeation flux values of different membranes are based on the first 5 h oxygen permeation measurements at different gradients. As presented in Figure 8, the highest oxygen permeation flux of 0.94 mL min−1 cm−2 under an air/He gradient is obtained for the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane. When switching the sweep gas from He to CO2, the oxygen permeation rate declines to 0.61 mL min−1 cm−2. This decrease can be mainly attributed to chemical adsorption of CO2 on the oxygen vacancy sites, which strongly hampers the surface exchange reaction at the interface of lattice oxygen and oxygen vacancy. The strong influence of different gas atmospheres on the oxygen surface exchange rates was previously discussed in detail [5,71,72]. Besides, the variation of oxygen partial pressures on the permeate side of the membrane may also lead to a decrease in the oxygen permeation flux upon changing the sweep gas. A similar response has been found for the other two membranes. The high oxygen permeation flux through Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ can be attributed to the good percolation network of the Ce0.9Pr0.1O2−δ and Nd0.5Sr0.5Fe0.9Cu0.1O3−δ phases as well as the membrane phase stability at high temperatures as discussed in the previous sections. Given that the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane shows the best performance, the oxygen permeation flux through the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane (a new membrane) was measured in the temperature range of 1023 K < T < 1223 K under air/He gradients. As shown in Figure 9, the oxygen permeation fluxes of the membrane increased with temperature, showing a thermal activation behavior. Both bulk diffusion and surface oxygen exchange reaction processes are enhanced by higher temperatures. The oxygen permeation flux of this new Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane reached 1.02 mL min−1 cm−2 at 1223 K under an air/He gradient. The deviation of the oxygen permeation flux with the previous value, as shown in Figure 8, is around 5% and reveals a promising reproducibility of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membranes. Slightly different surface morphologies and membrane thicknesses may result in the observed deviations. The activation energy of Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane is calculated to be 70 kJ mol−1, which is close to that of some other reported Nd-containing dual-phase membranes at similar conditions [49,50].
To gain insights into long-term CO2 durability and oxygen permeability, two additional Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membranes (thickness: 0.6 mm and 0.65 mm) were tested under air/He and air/CO2 gradients at 1223 K. As shown in Figure S2, the oxygen permeation flux through the 0.6 mm-thickness membrane reaches 0.97 mL min−1 cm−2 using He as the sweep gas, which has similar values as shown in Figure 8 and Figure 9. Switching He to CO2, the oxygen permeation rate goes down to 0.63 mL min−1 cm−2 and continues to decrease to a stable oxygen permeation flux around 0.3 mL min−1 cm−2 in the following 70 h period.
The reversibility of the oxygen permeability of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase has been also evaluated. Figure 10 depicts the changeability of the oxygen permeation flux through the 0.65 mm-thick membrane as a function of time by periodically changing He or CO2 as the sweep gas at 1223 K. A high and stable oxygen permeation flux of 0.95 mL min−1 cm−2 was reached using He as the sweep gas in the first 20 h. Similar to the behaviors shown in Figure S2, the oxygen permeation decreases to 0.2 mL min−1 cm−2 in the following 30 h exposure to CO2. Upon switching the sweep gas back to He, the oxygen permeation flux can be quickly recovered to almost the initial oxygen flux value, as illustrated in Figure 10. After two CO2 and He gas cycles, the oxygen permeation flux can still be recovered to 0.92 mL min−1 cm−2. The reversibility of the oxygen permeation fluxes during such alternating gas exposures suggests that the decrease in the oxygen permeation process was dominated by the CO2 sorption on the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane surface, rather than the chemical reaction with CO2 forming carbonates on the membrane surface which generally leads to a complete loss of oxygen permeation flux. For instance, no permeation was reported for a BaCo0.85Bi0.05Zr0.1O3−δ single phase membrane after using 10 vol% CO2-90 vol% He as a sweep gas due to the formation of BaCO3 [47]. No change of the crystal structures of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane is observed (as shown in Figure S3) before and after 70 h oxygen permeation under an air/CO2 gradient, revealing a high CO2 resistance. To further understand this behavior, the adsorption of CO2 on a Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane material was investigated experimentally by TGA when periodically changing the gas atmosphere between Ar and CO2 at 1223 K for 125 h. As clearly shown in Figure 11, the weight loss of Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ under CO2 (~2%) is significantly lower than that under the inert Ar gas (~4%) at 1223 K. When changing from Ar to CO2, a rapid weight gain to 98% of the initial weight is observed. During the CO2 exposure, a nearly constant weight was maintained. After switching back to Ar, a rapid weight loss to 96% occurred—observed after the first heating of Ar up to 1223 K. Additionally, the further switching of the gas atmosphere reveals a reproducible weight change between the above described values. All these observations suggest that the lattice oxygen releasing from the Ce0.9Pr0.1O2–δ–Nd0.5Sr0.5Fe0.9Cu0.1O3–δ membrane material is largely suppressed due to the strong CO2 adsorption or occupation of the oxygen vacancy sites by CO2. Generally, the surface exchange of oxygen and bulk diffusion of oxygen ions and electrons are the two rate-determining steps for the oxygen transport in MIEC membranes. From the reported data of various dual-phase membranes [50,65,66,67], the limitation of the oxygen transport process started to change from the oxygen bulk diffusion to surface oxygen exchange controlled when the thickness is less than 0.3 mm or 0.4 mm depending on the membrane material morphology, phase and operating conditions (gas atmosphere and temperature). Based on that, the bulk diffusion plays a dominant role in the oxygen permeation process through the 0.65 mm or 0.6 mm-thick membranes in this work. Decreasing the membrane thickness could be an effective way to further improve the oxygen permeation.
The oxygen permeabilitiesobtained within this work are compared with other dual-phase membranes under air/He and air/CO2 gradients in Table 1. Besides, the material costs for the representative membrane materials are also calculated, as shown in Table 1, based on the material costs of the used starting materials (metal source: nitrates) of dual-phase membrane materials summarized in Table S1. It can be seen that the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane has a higher oxygen permeation flux (0.94 mL min−1 cm−2) compared to several types of dual-phase membranes under an air/He gradient in similar conditions. The oxygen permeation flux in this study is improved by up to 45% in comparison with the best reported value of other Nd-containing dual-phase membranes in the literature under an air/He gradient at similar conditions (see Table 1 below). The oxygen permeation flux under an air/CO2 gradient is comparable to that of other Nd-containing dual-phase membranes. The material cost of the prepared Nd-containing dual-phase membrane material in this work is 1.76 EUR/g. It can be seen that Nd-containing membrane materials are much cheaper compared to other membrane materials (Sm-, Gd-, and Pr-containing samples). Therefore, the newly developed regenerative Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ membrane with lower material costs have high potential for separating oxygen from H2-containing and high CO2-containing atmospheres, respectively.

4. Conclusions

In this work, dense 40 wt % Ce0.9Pr0.1O2−δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δ dual-phase membranes are synthesized by a scalable one-pot method. The characterization results (XRD and SEM-EDXS) reveal a matching chemical compatibility between the fluorite-type phase (Ce0.9Pr0.1O2−δ) and perovskite-type phase (NdxSr1−xFe0.9Cu0.1O3−δ). The oxygen permeation flux under an air/He gradient is 45% higher than the best reported value of other Nd-containing dual-phase membranes in the literature at similar conditions. The oxygen permeation fluxes across a 0.6 mm thick Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane reach up to 1.02 mL min−1 cm−2 under an air/He gradient at T = 1223 K. Besides, a Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane (0.65 mm thickness) shows excellent long-term regenerative stability for 125 h. The significant poisoning effect of CO2 on the oxygen permeation fluxes through a Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane is mainly linked to the strong adsorption of CO2 to the membrane surface, which is experimentally verified by the TGA measurements with periodical changes of the gas atmosphere between Ar and CO2 at 1223 K for 125 h. The membranes show superior chemical resistance in the presence of CO2 and periodically regained their original structure for more than 500 h. In addition, the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane also demonstrates chemical durability in a H2-containing reducing atmosphere. Based on our findings, the newly developed Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ low-cost material appears to be a promising resource-efficient long lifetime membrane material for efficient high temperature oxygen transport membrane-based reactions owing to its structural stability in H2-containing and CO2 atmospheres together with a relatively high regenerative self-healing ability.

Supplementary Materials

The following are available online at https://www.mdpi.com/2077-0375/10/8/183/s1, Figure S1: Schematic diagram of the experimental setup for oxygen permeation measurements; Figure S2: Long-term oxygen permeation flux through a Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane at 1223 K under air/He or air/CO2 gradient. Test conditions: 150 mL min−1 synthetic air as the feed gas; 29 mL min−1 CO2 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 CO2) of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane after 70 h O2 permeation measurements as shown in Figure S2 under air/CO2 gradient (Bruker D8 Advance instrument with Cu-Kα1,2 radiation); Table S1: Summary of the starting material costs generally used in dual-phase membrane materials.

Author Contributions

Conceptualization: G.C.; Methodology: G.C., M.W., R.Y. and L.W.; Validation: Z.Z. and M.W., G.C.; Formal analysis: R.Y. and L.W.; Data curation: G.C., Z.Z., M.W., R.Y. and L.W.; Writing—original draft preparation: G.C.; Writing—review and editing, Z.Z., M.W., A.F. and A.W.; Supervision: A.F. and A.W.; Project administration: A.W.; Funding acquisition: A.W. All authors have read and agreed to the published version of the manuscript.

Funding

The authors received funding from Bundesministerium für Bildung und Forschung, the grant number is 03SFK2S3B.

Acknowledgments

This work is part of the project “Plasma-induced CO2-conversion” (PiCK, project number: 03SFK2S3B) and financially supported by the German Federal Ministry of Education and Research in the framework of the “Kopernikus projects for the Energiewende”. The authors are thankful to MSc. Binjie Tang for his support during experiments and discussions. The authors are thankful to Christine Stefani and Robert Dinnebier (Max Planck Institute for Solid State Research, Stuttgart) for the in situ PXRD measurements.

Conflicts of Interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

References

  1. Ma, T.; Han, N.; Meng, B.; Yang, N.; Zhu, Z.; Liu, S. Enhancing oxygen permeation via the incorporation of silver inside perovskite oxide membranes. Processes 2019, 7, 199. [Google Scholar] [CrossRef][Green Version]
  2. Zhu, X.; Yang, W. Critical factors affecting oxygen permeation through dual-phase membranes. In Membrane Science and Technology; Oyama, S.T., Stagg-Williams, S.M., Eds.; Elsevier: Amsterdam, The Netherlands, 2011; Volume 14, Chapter 12; pp. 275–293. [Google Scholar] [CrossRef]
  3. Shi, L.; Wang, S.; Lu, T.; He, Y.; Yan, D.; Lan, Q.; Xie, Z.; Wang, H.; Boubeche, M.; Luo, H. Effects of Al content on the oxygen permeability through dual-phase membrane 60Ce0.9Pr0.1O2-δ–40Pr0.6Sr0.4Fe1-x AlxO3-δ. Ceram. Int. 2019, 45, 20033–20039. [Google Scholar] [CrossRef][Green Version]
  4. Zhang, C.; Sunarso, J.; Liu, S. Designing CO2-resistant oxygen-selective mixed ionic-electronic conducting membranes: Guidelines, recent advances, and forward directions. Chem. Soc. Rev. 2017, 46, 2941–3005. [Google Scholar] [CrossRef] [PubMed]
  5. Sunarso, J.; Baumann, S.; Serra, J.M.; Meulenberg, W.A.; Liu, S.; Lin, J.Y.; Diniz da Costa, J.C. Mixed ionic-electronic conducting (MIEC) ceramic-based membranes for oxygen separation. J. Membr. Sci. 2008, 320, 13–41. [Google Scholar] [CrossRef]
  6. Chen, G.; Tang, B.; Widenmeyer, M.; Wang, L.; Feldhoff, A.; Weidenkaff, A. Novel CO2-tolerant dual-phase Ce0.9Pr0.1O2-δ–La0.5Sr0.5Fe0.9Cu0.1O3-δ membranes with high oxygen permeability. J. Membr. Sci. 2020, 595, 117530. [Google Scholar] [CrossRef]
  7. Geffroy, P.-M.; Blond, E.; Richet, N.; Chartier, T. Understanding and identifying the oxygen transport mechanisms through a mixed-conductor membrane. Chem. Eng. Sci. 2017, 162, 245–261. [Google Scholar] [CrossRef]
  8. Widenmeyer, M.; Wiegers, K.-S.; Chen, G.; Yoon, S.; Feldhoff, A.; Weidenkaff, A. Engineering of oxygen pathways for better oxygen permeability in Cr-substituted Ba2In2O5 membranes. J. Membr. Sci. 2020, 595, 117558. [Google Scholar] [CrossRef]
  9. Efimov, K.; Klande, T.; Juditzki, N.; Feldhoff, A. Ca-Containing CO2-tolerant perovskite materials for oxygen separation. J. Membr. Sci. 2012, 389, 205–215. [Google Scholar] [CrossRef]
  10. Wang, Y.; Cheng, H.; Chen, S.; Zhao, H.; Lu, X.; Xu, Q. CO2-Tolerance and oxygen permeability of novel cobalt-free mixed-conductor oxygen-permeable Pr0.6Sr0.4Fe1-xNbxO3-δ membranes. Ceram. Int. 2017, 43, 13791–13799. [Google Scholar] [CrossRef]
  11. Zhang, Z.; Chena, D.; Dong, F.; Xu, X.; Hao, Y.; Shao, Z. Understanding the doping effect toward the design of CO2-tolerant perovskite membranes with enhanced oxygen permeability. J. Membr. Sci. 2016, 519, 11–21. [Google Scholar] [CrossRef]
  12. Yi, J.; Schroeder, M.; Martin, M. CO2-tolerant and cobalt-Free SrFe0.8Nb0.2O3-δ perovskite membrane for oxygen separation. Chem. Mater. 2013, 25, 815–817. [Google Scholar] [CrossRef]
  13. Du, M.; Liao, K.; Lu, Q.; Shao, Z. Recent advances in the interface engineering of solid-state Li-ion batteries with artificial buffer layers: Challenges, materials, construction, and characterization. Energy Environ. Sci. 2019, 12, 1780–1804. [Google Scholar] [CrossRef]
  14. Li, R.; Liao, K.; Zhou, W.; Li, X.; Meng, D.; Cai, R.; Shao, Z. Realizing fourfold enhancement in conductivity of perovskite Li0.33La0.557TiO3 electrolyte membrane via a Sr and Ta co-doping strategy. J. Membr. Sci. 2019, 582, 194–202. [Google Scholar] [CrossRef]
  15. Zou, X.; Lu, Q.; Zhong, Y.; Liao, K.; Zhou, W.; Shao, Z. Flexible, flame-resistant, and dendrite-impermeable gel-polymer electrolyte for Li-O2/Air batteries workable under hurdle conditions. Small 2018, 14, 1801798. [Google Scholar] [CrossRef] [PubMed]
  16. Dueñas, D.M.A.; Chen, G.; Weidenkaff, A.; Sata, N.; Han, F.; Schiller, G.; Costa, R.; Friedrich, A.K. Synthesis and evaluation of the A-Site deficient perovskite La0.65Sr0.3Cr0.85Ni0.15O3-δ as fuel electrode for high temperature Co-electrolysis enhanced by in situ exsolution of Ni nanoparticles. ECS Trans. 2019, 91, 1751–1760. [Google Scholar] [CrossRef]
  17. Jacobson, A.J. Materials for solid oxide fuel cells. Chem. Mater. 2010, 22, 660–674. [Google Scholar] [CrossRef]
  18. Xu, X.; Bi, L.; Zhao, X.S. Highly-Conductive proton-conducting electrolyte membranes with a low sintering temperature for solid oxide fuel cells. J. Membr. Sci. 2018, 558, 17–25. [Google Scholar] [CrossRef]
  19. Suntivich, J.; May, K.J.; Gasteiger, H.A.; Goodenough, J.B.; Shao-Horn, Y. A perovskite oxide optimized for oxygen evolution catalysis from molecular orbital principles. Science 2011, 334, 1383–1385. [Google Scholar] [CrossRef]
  20. Fang, J.; Jin, X.; Huang, K. Life cycle analysis of a combined CO2 capture and conversion membrane reactor. J. Membr. Sci. 2018, 549, 142–150. [Google Scholar] [CrossRef]
  21. Plazaola, A.A.; Cruellas, A.; Liu, Y.; Porras, N.B.; Tanaka, D.A.P.; Annaland, M.V.S.; Gallucci, F. Mixed ionic-electronic conducting membranes (MIEC) for their application in membrane reactors: a review. Processes 2019, 7, 128. [Google Scholar] [CrossRef][Green Version]
  22. Jin, W.; Zhang, C.; Chang, X.; Fan, Y.; Xing, W.; Xu, N. Efficient catalytic decomposition of CO2 to CO and O2 over Pd/Mixed-conducting oxide catalyst in an oxygen-permeable membrane reactor. Environ. Sci. Technol. 2008, 42, 3064–3068. [Google Scholar] [CrossRef] [PubMed]
  23. Wu, X.-Y.; Ghoniem, A.F. Mixed ionic-electronic conducting (MIEC) membranes for thermochemical reduction of CO2: A review. Prog. Energy Combust. Sci. 2019, 74, 1–30. [Google Scholar] [CrossRef]
  24. Snoeckx, R.; Bogaerts, A. Plasma technology—A novel solution for CO2 conversion? Chem. Soc. Rev. 2017, 46, 5805–5863. [Google Scholar] [CrossRef] [PubMed][Green Version]
  25. Stadler, H.; Beggel, F.; Habermehl, M.; Persigehl, B.; Kneer, R.; Modigell, M.; Jeschke, P. Oxyfuel coal combustion by efficient integration of oxygen transport membranes. Int. J. Greenh. Gas Control 2011, 5, 7–15. [Google Scholar] [CrossRef]
  26. Schiestel, T.; Kilgus, M.; Peter, S.; Caspary, K.; Wang, H.; Caro, J. Hollow fibre perovskite membranes for oxygen separation. J. Membr. Sci. 2005, 258, 1–4. [Google Scholar] [CrossRef]
  27. Chen, G.; Widenmeyer, M.; Tang, B.; Kaeswurm, L.; Wang, L.; Feldhoff, A.; Weidenkaff, A. A CO and CO 2 tolerating (La0.9Ca0.1)2(Ni0.75Cu0.25)O4+ δ Ruddlesden-Popper membrane for oxygen separation. Front. Chem. Sci. Eng. 2020, 14, 405–414. [Google Scholar] [CrossRef]
  28. Buck, F.; Kistner, I.; Rösler, C.; Schulz, A.; Walker, M.; Tovar, G.E.M.; Schiestel, T.; Tovar, G. Einsatz von perowskitischen Hohlfasermembranen in einem Mikrowellenplasma. Chem. Ing. Tech. 2019, 91, 1117–1122. [Google Scholar] [CrossRef]
  29. Chen, G.; Buck, F.; Kistner, I.; Widenmeyer, M.; Schiestel, T.; Schulz, A.; Walker, M.; Weidenkaff, A. A novel plasma-assisted hollow fiber membrane concept for efficiently separating oxygen from CO in a CO2 plasma. Chem. Eng. J. 2020, 392, 123699. [Google Scholar] [CrossRef]
  30. Chen, G.; Britun, N.; Godfroid, T.; Delplancke-Ogletree, M.; Snyders, R. Role of plasma catalysis in the microwave plasma-assisted conversion of CO2. In Green Chemical Processing and Synthesis; Karame, I., Srour, H., Eds.; IntechOpen: London, UK, 2017. [Google Scholar] [CrossRef][Green Version]
  31. Chen, G.; Georgieva, V.; Godfroid, T.; Snyders, R.; Delplancke-Ogletree, M.-P. Plasma assisted catalytic decomposition of CO2. Appl. Catal. B Environ. 2016, 190, 115–124. [Google Scholar] [CrossRef]
  32. Chen, G.; Godfroid, T.; Georgieva, V.; Britun, N.; Delplancke-Ogletree, M.-P.; Snyders, R. Plasma-catalytic conversion of CO2 and CO2/H2O in a surface-wave sustained microwave discharge. Appl. Catal. B Environ. 2017, 214, 114–125. [Google Scholar] [CrossRef]
  33. Chen, G.; Wang, L.; Godfroid, T.; Snyders, R. Progress in plasma-assisted catalysis for carbon dioxide reduction. In Plasma Chemistry and Gas Conversion; Britun, N., Silva, T., Eds.; IntechOpen: London, UK, 2018. [Google Scholar] [CrossRef][Green Version]
  34. Li, X.; Kerstiens, T.; Markus, T. Oxygen permeability and phase stability of Ba0.5Sr0.5Co0.8Fe0.2O3-δ perovskite at intermediate temperatures. J. Membr. Sci. 2013, 438, 83–89. [Google Scholar] [CrossRef]
  35. Park, J.H.; Kim, J.P.; Son, S.H. Oxygen permeation and stability of Ba0.5Sr0.5Co0.8Fe0.2O3-δ membrane according to trace elements and oxygen partial pressure in synthetic air. Energy Procedia 2009, 1, 369–374. [Google Scholar] [CrossRef][Green Version]
  36. Alaee, M.A.; Movahednia, M.M.; Mohammadi, T. Correction to effect of Ba content on oxygen permeation performance of BaxSr1-xCo0.8Fe0.2O3-δ (x = 0.2, 0.5, and 0.8) Perovskite-Type Membrane. J. Chem. Eng. Data 2018, 63, 857. [Google Scholar] [CrossRef][Green Version]
  37. Zhu, X.; Yang, W. Microstructural and interfacial designs of oxygen-permeable membranes for oxygen separation and reaction-separation coupling. Adv. Mater. 2019, 31, e1902547. [Google Scholar] [CrossRef]
  38. Li, K.; Zhao, H.; Lü, Y.; Ma, Y.; Du, Z.; Zhang, Z. High CO2 tolerance oxygen permeation membranes BaFe0.95-xCa0.05TixO3-δ. J. Membr. Sci. 2018, 550, 302–312. [Google Scholar] [CrossRef]
  39. Liu, J.; Cheng, H.; Jiang, B.; Lu, X.; Ding, W. Effects of tantalum content on the structure stability and oxygen permeability of BaCo0.7Fe0.3-xTaxO3-δ ceramic membrane. Int. J. Hydrogen Energy 2013, 38, 11090–11096. [Google Scholar] [CrossRef]
  40. Chen, G.; Liu, W.; Widenmeyer, M.; Ying, P.; Dou, M.; Xie, W.; Bubeck, C.; Wang, L.; Fyta, M.; Feldhoff, A.; et al. High flux and CO2-resistance of La0.6Ca0.4Co1-xFexO3-δ oxygen-transporting membranes. J. Membr. Sci. 2019, 590, 117082. [Google Scholar] [CrossRef]
  41. Lu, Y.; Zhao, H.; Chang, X.; Du, X.; Li, K.; Ma, Y.; Yi, S.; Du, Z.; Zheng, K.; Świerczek, K. Novel cobalt-free BaFe1-xGdxO3-δ perovskite membranes for oxygen separation. J. Mater. Chem. A 2016, 4, 10454–10466. [Google Scholar] [CrossRef][Green Version]
  42. Yang, Z.; Martynczuk, J.; Efimov, K.; Harvey, A.S.; Infortuna, A.; Kocher, P.; Gauckler, L.J. Oxygen-vacancy-related structural phase transition of Ba0.8Sr0.2Co0.8 Fe0.2O3-δ. Chem. Mater. 2011, 23, 3169–3175. [Google Scholar] [CrossRef]
  43. Guironnet, L.; Geffroy, P.-M.; Tessier-Doyen, N.; Boulle, A.; Richet, N.; Chartier, T. The surface roughness effect on electrochemical properties of La0.5Sr0.5Fe0.7Ga0.3O3-δ perovskite for oxygen transport membranes. J. Membr. Sci. 2019, 588, 117199. [Google Scholar] [CrossRef]
  44. Li, T.; Kamhangdatepon, T.; Wang, B.; Hartley, U.W.; Li, K.; Khamhangdatepon, T. New bio-inspired design for high-performance and highly robust La0.6Sr0.4Co0.2Fe0.8O3-δ membranes for oxygen permeation. J. Membr. Sci. 2019, 578, 203–208. [Google Scholar] [CrossRef]
  45. Garcia-Fayos, J.; Ruhl, R.; Navarrete, L.; Serra, J.M.; Bouwmeester, H.J.M. Enhancing oxygen permeation through Fe2NiO4–Ce0.8Tb0.2O2-δ composite membranes using porous layers activated with Pr6O11 nanoparticles. J. Mater. Chem. A 2018, 6, 1201–1209. [Google Scholar] [CrossRef]
  46. Magnone, E.; Chae, J.; Park, J.H. Synthesis and oxygen permeation properties of Ce0.8Sm0.2O2-d—Sm1-xSrxCu0.2Fe0.8O3-d dual-phase ceramic membranes: effect of strontium contents and Pd coating layer. Ceram. Int. 2018, 44, 12948–12956. [Google Scholar] [CrossRef]
  47. Fang, W.; Zhang, Y.; Gao, J.; Chen, C. Oxygen permeability of asymmetric membrane of functional La0.8 Sr0.2Cr0.5Fe0.5O3-δ(LSCrF)–Zr0.8Y0.2O2-δ(YSZ) supported on porous YSZ. Ceram. Int. 2014, 40, 799–803. [Google Scholar] [CrossRef]
  48. Shi, L.; Wang, S.; Lu, T.; He, Y.; Yan, N.; Lan, Q.; Xie, Z.; Wang, H.; Li, M.-R.; Caro, J.; et al. High CO2-tolerance oxygen permeation dual-phase membranes Ce0.9Pr0.1O2-δ–Pr0.6Sr0.4Fe0.8Al0.2O3-δ. J. Alloy. Compd. 2019, 806, 500–509. [Google Scholar] [CrossRef][Green Version]
  49. Luo, H.; Klande, T.; Cao, Z.; Liang, F.; Wang, H.; Caro, J. A CO2-Stable reduction-tolerant Nd-containing dual phase membrane for oxyfuel CO2 capture. J. Mater. Chem. A 2014, 2, 7780–7787. [Google Scholar] [CrossRef][Green Version]
  50. He, Y.; Shi, L.; Wu, F.; Xie, W.; Wang, S.; Yan, N.; Liu, P.; Li, M.-R.; Caro, J.; Luo, H. A novel dual phase membrane 40 wt % Nd0.6Sr0.4CoO3-δ–60 wt % Ce0.9Nd0.1O2-δ: design, synthesis and properties. J. Mater. Chem. A 2018, 6, 84–92. [Google Scholar] [CrossRef]
  51. Luo, H.; Jiang, H.; Efimov, K.; Caro, J.; Wang, H. Influence of the preparation methods on the microstructure and oxygen permeability of a CO2-stable dual phase membrane. AIChE J. 2010, 57, 2738–2745. [Google Scholar] [CrossRef]
  52. Partovi, K.; Rüscher, C.H.; Steinbach, F.; Caro, J. Enhanced oxygen permeability of novel Cu-containing CO2-tolerant dual-phase membranes. J. Membr. Sci. 2016, 503, 158–165. [Google Scholar] [CrossRef]
  53. Liang, F.; Luo, H.; Partovi, K.; Ravkina, O.; Cao, Z.; Liu, Y.; Caro, J. A novel CO2-stable dual phase membrane with high oxygen permeability. Chem. Commun. 2014, 50, 2451–2454. [Google Scholar] [CrossRef][Green Version]
  54. Fang, W.; Steinbach, F.; Chen, C.; Feldhoff, A. An Approach to enhance the CO2 tolerance of fluorite-perovskite dual-phase oxygen-transporting membrane. Chem. Mater. 2015, 27, 7820–7826. [Google Scholar] [CrossRef]
  55. Gili, A.; Bischoff, B.; Simon, U.; Schmidt, F.; Kober, D.; Görke, O.; Bekheet, M.F.; Gurlo, A. Ceria-based dual-phase membranes for high-temperature carbon dioxide separation: effect of iron doping and pore generation with MgO template. Membranes 2019, 9, 108. [Google Scholar] [CrossRef] [PubMed][Green Version]
  56. Fang, W.; Liang, F.; Cao, Z.; Steinbach, F.; Feldhoff, A. A mixed ionic and electronic conducting dual-phase membrane with high oxygen permeability. Angew. Chem. Int. Ed. 2015, 54, 4847–4850. [Google Scholar] [CrossRef]
  57. Liu, C.; Cheng, H.; Yan, G.; Zhao, H.; Lu, X.; Wang, P. Effects of B-site Nb doping on the CO2 resistance and rate-controlling step of Ce0.8Gd0.2O2-δ—Pr0.6Sr0.4Co0.5Fe0.5O3-δ dual-phase membranes. J. Mater. Sci. 2018, 53, 11962–11976. [Google Scholar] [CrossRef]
  58. Luo, H.; Feldhoff, A.; Wang, H.; Efimov, K.; Jiang, H.; Caro, J. CO2-Stable and cobalt-free dual-phase membrane for oxygen separation. Angew. Chem. Int. Ed. 2010, 50, 759–763. [Google Scholar] [CrossRef]
  59. Du, Z.; Ma, Y.; Zhao, H.; Li, K.; Lu, Y. High CO2-tolerant and cobalt-free dual-phase membranes for pure oxygen separation. J. Membr. Sci. 2019, 574, 243–251. [Google Scholar] [CrossRef]
  60. Zhu, X.; Liu, H.; Cong, Y.; Yang, W. Novel dual-phase membranes for CO2 capture via an oxyfuel route. Chem. Commun. 2012, 48, 251–253. [Google Scholar] [CrossRef]
  61. Li, C.; Li, W.; Chew, J.; Liu, S.; Zhu, X.; Sunarso, J. Rate determining step in SDC-SSAF dual-phase oxygen permeation membrane. J. Membr. Sci. 2019, 573, 628–638. [Google Scholar] [CrossRef]
  62. Nan, N.; Wei, Q.; Tian, H.; Zhang, S.; Zhu, Z.; Liu, J.; Liu, S. Highly stable dual-phase membrane based on Ce0.9Gd0.1O2-δ–La2NiO4-δ for oxygen permeation under pure CO2 atmosphere. Energy Technol. 2019, 7, 1800701. [Google Scholar] [CrossRef]
  63. Garcia-Fayos, J.; Balaguer, M.; Baumann, S.; Serra, J.M. Dual-phase membrane based on LaCo0.2Ni0.4Fe0.4 O3-x-Ce0.8Gd0.2O2-x composition for oxygen permeation under CO2/SO2-rich gas environments. J. Membr. Sci. 2018, 548, 117–124. [Google Scholar] [CrossRef]
  64. Zhang, Z.; Zhou, W.; Chen, Y.; Chena, D.; Chen, J.; Liu, S.; Jin, W.; Shao, Z. Novel approach for developing dual-phase ceramic membranes for oxygen separation through beneficial phase reaction. ACS Appl. Mater. Interfaces 2015, 7, 22918–22926. [Google Scholar] [CrossRef] [PubMed]
  65. Wang, S.; Shi, L.; Xie, Z.; He, Y.; Yan, D.; Li, M.-R.; Caro, J.; Luo, H. High-flux dual-phase percolation membrane for oxygen separation. J. Eur. Ceram. Soc. 2019, 39, 4882–4890. [Google Scholar] [CrossRef][Green Version]
  66. Cheng, H.; Zhang, N.; Xiong, X.; Lu, X.; Zhao, H.; Li, S.; Zhou, Z. Synthesis, Oxygen permeation, and CO2-tolerance properties of Ce0.8Gd0.2O2-δ—Ba0.95La0.05Fe1-xNbxO3-δ dual-phase membranes. ACS Sustain. Chem. Eng. 2015, 3, 1982–1992. [Google Scholar] [CrossRef]
  67. Zhang, G.; Bao, X.; Zeng, F.; Minh, N.Q.; Wang, S. Preparation and characterization of Ce0.8Sm0.2O1.9—La0.8 Sr0.2Cr0.5Fe0.5O3-d dual-phase membranes for oxygen permeation. J. Materiomics 2020, 6, 224–231. [Google Scholar] [CrossRef]
  68. Omar, S.; Wachsman, E.D.; Jones, J.L.; Nino, J.C. Crystal structure-ionic conductivity relationships in doped ceria systems. J. Am. Ceram. Soc. 2009, 92, 2674–2681. [Google Scholar] [CrossRef]
  69. Bocher, L.; Robert, R.; Aguirre, M.H.; Malo, S.; Hébert, S.; Maignan, A.; Weidenkaff, A. Thermoelectric and magnetic properties of perovskite-type manganate phases synthesised by an Ultrasonic Spray Combustion (USC) method. J. Sol. State Sci. 2008, 10, 496–501. [Google Scholar] [CrossRef]
  70. Stevenson, J.W.; Armstrong, T.R.; Carneim, R.D.; Pederson, L.R.; Weber, W.J. Electrochemical properties of mixed conducting perovskites La1-xMxCo1-yFeyO3-δ (M = Sr, Ba, Ca). J. Electrochem. Soc. 1996, 143, 2722–2729. [Google Scholar] [CrossRef]
  71. Elshof, J.E.T.; Bouwmeester, H.J.; Verweij, H. Oxygen transport through La1-xSrxFeO3-δ membranes II. Permeation in air/CO, CO2 gradients. Solid State Ionics 1996, 89, 81–92. [Google Scholar] [CrossRef][Green Version]
  72. Khromushin, I.V.; Aksenova, T.; Zhotabaev, Z. Mechanism of gas-solid exchange processes for some perovskites. Solid State Ionics 2003, 162, 37–40. [Google Scholar] [CrossRef]
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Figure 1. XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) dual-phase membranes. (a) Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (c) Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cub;;0.1O3−δ; (d) Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (e) Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (f) Nd0.8Sr0.2Fe0.9Cu0.1O3−δ; (g) Ce0.9Pr0.1O2−δ. *: impurity reflection.
Figure 1. XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) dual-phase membranes. (a) Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (c) Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cub;;0.1O3−δ; (d) Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (e) Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (f) Nd0.8Sr0.2Fe0.9Cu0.1O3−δ; (g) Ce0.9Pr0.1O2−δ. *: impurity reflection.
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Figure 2. SEM and the corresponding energy-dispersive X-ray spectroscopy (EDXS) images of fresh unpolished Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ dual-phase membranes. (a) Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (c) Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ. Contribution to the EDXS mapping data (d–f) resulting from the fluorite phases (Ce Lα and Pr Lα) are marked in green and in red for the perovskite-type phases (Nd Lα, Sr Lα, Fe Kα and Cu Lα).
Figure 2. SEM and the corresponding energy-dispersive X-ray spectroscopy (EDXS) images of fresh unpolished Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ dual-phase membranes. (a) Ce0.9Pr0.1O2−δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (c) Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ. Contribution to the EDXS mapping data (d–f) resulting from the fluorite phases (Ce Lα and Pr Lα) are marked in green and in red for the perovskite-type phases (Nd Lα, Sr Lα, Fe Kα and Cu Lα).
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Figure 3. Thermogravimetric (TG) curves of Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) dual-phase membranes under flowing (a) Ar, (b) CO2, (c) air and (d) 5 vol% H2-95 vol% Ar atmospheres (heating rate: 10 K min−1).
Figure 3. Thermogravimetric (TG) curves of Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) dual-phase membranes under flowing (a) Ar, (b) CO2, (c) air and (d) 5 vol% H2-95 vol% Ar atmospheres (heating rate: 10 K min−1).
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Figure 4. XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) samples after TGA measurements were made under a CO2 atmosphere.
Figure 4. XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) samples after TGA measurements were made under a CO2 atmosphere.
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Figure 5. XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) bulk samples before and after TGA measurements under a 5 vol% H2-95 vol% Ar atmosphere.
Figure 5. XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1–xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) bulk samples before and after TGA measurements under a 5 vol% H2-95 vol% Ar atmosphere.
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Figure 6. In situ XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ powders in air: (a) Ce0.9Pr0.1O2–δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (c) Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ.
Figure 6. In situ XRD patterns of Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ powders in air: (a) Ce0.9Pr0.1O2–δ–Nd0.2Sr0.8Fe0.9Cu0.1O3−δ; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ; (c) Ce0.9Pr0.1O2−δ–Nd0.8Sr0.2Fe0.9Cu0.1O3−δ.
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Figure 7. XRD patterns of the Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) powder samples after exposure to the CO2 atmosphere: (a) at 1173 K for 100 h; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ sample at different temperatures for 2 h; (c) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ sample for different times at 1173 K.
Figure 7. XRD patterns of the Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) powder samples after exposure to the CO2 atmosphere: (a) at 1173 K for 100 h; (b) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ sample at different temperatures for 2 h; (c) Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ sample for different times at 1173 K.
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Figure 8. Oxygen permeation fluxes through the Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) membranes (thickness: 0.6 mm) under air/He and air/CO2 gradients at 1223 K.
Figure 8. Oxygen permeation fluxes through the Ce0.9Pr0.1O2−δ–NdxSr1−xFe0.9Cu0.1O3−δ (x = 0.2, 0.5, 0.8) membranes (thickness: 0.6 mm) under air/He and air/CO2 gradients at 1223 K.
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Figure 9. Oxygen permeation fluxes (a) and its Arrhenius plot (b) of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane (thickness: 0.6 mm) under an air/He gradient.
Figure 9. Oxygen permeation fluxes (a) and its Arrhenius plot (b) of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase membrane (thickness: 0.6 mm) under an air/He gradient.
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Figure 10. Long-term oxygen permeation flux through a Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane at 1223 K under an air/He or air/CO2 gradient. Test conditions: 0.65 mm membrane thickness; 150 mL min−1 synthetic air as the feed gas; 29 mL min−1 CO2 as the sweep gas; 1 mL min−1 Ne as an internal standard gas.
Figure 10. Long-term oxygen permeation flux through a Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ membrane at 1223 K under an air/He or air/CO2 gradient. Test conditions: 0.65 mm membrane thickness; 150 mL min−1 synthetic air as the feed gas; 29 mL min−1 CO2 as the sweep gas; 1 mL min−1 Ne as an internal standard gas.
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Figure 11. TG curve of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase powder material while periodically changing the gas atmosphere between Ar and CO2 at 1223 K.
Figure 11. TG curve of the Ce0.9Pr0.1O2−δ–Nd0.5Sr0.5Fe0.9Cu0.1O3−δ dual-phase powder material while periodically changing the gas atmosphere between Ar and CO2 at 1223 K.
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Table
Table 1. Summary of the reported promising oxygen permeation fluxes of various dual-phase membranes.
Table 1. Summary of the reported promising oxygen permeation fluxes of various dual-phase membranes.
SampleJ(O2) (air/He)
(mL min−1 cm−2)		J(O2) (air/CO2)
(mL min−1 cm−2)		d (mm)T
(K)		J(O2) (air/CO2)
Stability (h)		Material cost
(EUR/g)		Ref.
CPO-NSFCO0.970.320.61223701.76This work (Figure S2)
CPO-NSFCO0.940.610.6122351.76This work (Figure 8)
CPO-NSFCO1.02--0.61223101.76This work (Figure 9)
CPO-NSFCO0.940.20.651223125 1.76This work (Figure 10)
CNO-NSFO0.260.210.612231201.70[49]
CNO-NSCO0.650.550.612231501.89[50]
CSO-SSCFO1.010.70.61223502.81[52]
CPO-PSFCO0.840.70.612234002.23[53]
CGO-PSCFO0.60.450.51173----[55]
CGCO-LCFO0.870.70.51223----[56]
LCO-30LSFO0.320.190.61173 100--[59]
LCCO-30LSFO0.450.270.61173100--[59]
CSO-SCMCO0.40.340.5117375--[60]
CPO-NSFCO: 40wt % Ce0.9Pr0.1O2−δ–60wt % Nd00.5Sr0.5Fe0.9Cu0.1O3−δ. CNO-NSFO: 60 wt %Ce0.9 Nd0.1O2−δ–40 wt % Nd0.6Sr0.4FeO3−δ. CNO-NSCO: 60 wt % Ce0.9Nd0.1O2−δ–40 wt % Nd0.6Sr0.4CoO3−δ. CGO-PSCFO: 60 wt % Ce0.8Gd0.2O2–δ– 40 wt % Pr0.6Sr0.4Co0.5Fe0.5O3–δ. CSO-SSCFO: 60 wt % Ce0.8Sm0.2O2−δ–40 wt % Sm0.3Sr0.7Cu0.2Fe0.8O3−δ. CPO-PSFCO: 60 wt % Ce0.9Pr0.1O2–δ–40 wt % Pr0.6Sr0.4Fe0.5Co0.5O3−δ. LDCO-LSFO: 70 wt % La0.15Ce0.85O2−δ–30 wt % La0.15Sr0.85FeO3−δ. CSO-SCMCO: 75wt % Ce0.8Sm0.2O1.9–25wt % Sm0.8Ca0.2Mn0.5Co0.5O3CGCO-LCFO: 75 wt % Ce0.85Gd0.1Cu0.05O2−δ–25 wt % La0.6Ca0.4FeO3−δ. CPO-NSFCO: 40wt % Ce0.9Pr0.1O2−δ–60wt % Nd0.5Sr0.5Fe0.9Cu0.1O3−δ. LCCO-LSFO: 70 wt % La0.15Ce0.8Cu0.05O2−δ –30 wt % La0.15Sr0.85FeO3−δ.

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Chen, G.; Zhao, Z.; Widenmeyer, M.; Yan, R.; Wang, L.; Feldhoff, A.; Weidenkaff, A. Synthesis and Characterization of 40 wt % Ce0.9Pr0.1O2–δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δ Dual-Phase Membranes for Efficient Oxygen Separation. Membranes 2020, 10, 183. https://doi.org/10.3390/membranes10080183

AMA Style

Chen G, Zhao Z, Widenmeyer M, Yan R, Wang L, Feldhoff A, Weidenkaff A. Synthesis and Characterization of 40 wt % Ce0.9Pr0.1O2–δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δ Dual-Phase Membranes for Efficient Oxygen Separation. Membranes. 2020; 10(8):183. https://doi.org/10.3390/membranes10080183

Chicago/Turabian Style

Chen, Guoxing, Zhijun Zhao, Marc Widenmeyer, Ruijuan Yan, Ling Wang, Armin Feldhoff, and Anke Weidenkaff. 2020. "Synthesis and Characterization of 40 wt % Ce0.9Pr0.1O2–δ–60 wt % NdxSr1−xFe0.9Cu0.1O3−δ Dual-Phase Membranes for Efficient Oxygen Separation" Membranes 10, no. 8: 183. https://doi.org/10.3390/membranes10080183

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