Publication date: October 2025
Source: Journal of Colloid and Interface Science, Volume 695
Author(s): Xue Yang, Donghui Cui, Yu Liu, Yuexin Xiang, Fengyan Li
Publication date: October 2025
Source: Journal of Colloid and Interface Science, Volume 695
Author(s): Xue Yang, Donghui Cui, Yu Liu, Yuexin Xiang, Fengyan Li
A piezoelectric interlayer design between an Na3Zr2Si2PO12 solid electrolyte and sodium metal is demonstrated to solve the interfacial issues against low-temperature solid-state sodium batteries. A piezoelectric ZnO layer proves a favorable interlayer with matched modulus, high Na-adhesion, sufficient piezoelectricity to thoroughly reduce the interfacial resistance and promote a quasi-solid-state Na2MnFe(CN)6-based full cell operating at a harsh condition of 0 °C.
Solid-state sodium (Na) batteries (SSNBs) hold great promise but suffer from several major issues, such as high interfacial resistance at the solid electrolyte/electrode interface and Na metal dendrite growth. To address these issues, a piezoelectric interlayer design for an Na3Zr2Si2PO12 (NZSP) solid electrolyte is proposed herein. Two typical piezoelectric films, AlN and ZnO, coated onto NZSP function as interlayers designed to generate a local stress-induced field for alleviating interfacial charge aggregation coupling stress concentration and promoting uniform Na plating. The results reveal that the interlayer (ZnO) with matched modulus, high Na-adhesion, and sufficient piezoelectricity can provide a favorable interphase. Low interfacial resistances of 91 and 239 Ω cm2 are achieved for the ZnO layer at 30 and 0 °C, respectively, which are notably lower than those for bare NZSP. Moreover, steady Na plating/stripping cycles are rendered over 850 and 4900 h at 0 and 30 °C, respectively. The superior anodic performance is further manifested in an Na2MnFe(CN)6-based full cell which delivers discharge capacities of 125 mA h g−1 over 1600 cycles at 30 °C and 90 mA h g−1 over 500 cycles at 0 °C. A new interlayer-design insight is clearly demonstrated for SSNBs breaking low-temperature limits.



A nanostructured carbon with high specific surface area (SSA), tunable pore structure, superior electrical conductivity, mechanically robust framework, and high chemical stability is an important requirement for electrochemical energy storage. Porous graphene fabricated by chemical activation and liquid etching has a high surface area but very limited volume of electrochemically accessible mesopores. Herein, an effective strategy of in situ formation of hierarchically mesoporous oxide templates with small pores induced by Kirkendall diffusion and large pores attributed to evaporation of deliberately introduced volatile metal is proposed for chemical vapor deposition assembly of porous graphene frameworks (PGFs). The PGFs inherit the hierarchical mesoporous structure of the templates. A high SSA of 1448 m2 g−1, 91.6% of which is contributed by mesopores, and a mesopore volume of 2.40 cm3 g−1 are attained for PGFs serving as reservoirs of ions or active materials in electrochemical energy storage applications. When the PGFs are applied in lithium-sulfur batteries, a very high sulfur utilization of 71% and a very low fading rate of ≈0.04% per cycle after the second cycle are achieved at a current rate of 1.0 C. This work provides a general strategy for the rational construction of mesoporous structures induced by a volatile metal, with a view toward the design of hierarchical nanomaterials for advanced energy storage.
Porous graphene frameworks (PGFs) are fabricated on hierarchically mesoporous oxide templates with small pores induced by Kirkendall diffusion and large pores attributed to evaporation of a deliberately introduced volatile metal. A high specific surface area of 1448 m2 g−1 and large mesopore volume of 2.40 cm3 g−1 are attained for PGFs serving as reservoirs of ions or active materials in lithium-sulfur batteries.
The hydrogenation of furfural to furfuryl alcohol was performed in the presence of a Co/SBA-15 catalyst. High selectivity (96 %) at a conversion higher than 95 % is reported over this catalytic system. As the conversion of furfural to furfuryl alcohol occurs over metallic Co sites, the effect of reduction temperature, H2 pressure, and reaction temperature were studied. Optimum reaction conditions were: 150 °C, 1.5 h, 2.0 MPa of H2. The catalyst was recyclable, and furfuryl alcohol was recovered with a purity higher than 90 %. The effect of the solvent concentration was also studied. With a minimum of 50 wt % of solvent, the selectivity to furfuryl alcohol and the conversion of furfural remained high (both over 80 %). Likewise, the activity of the catalyst is maintained even in pure furfural, which confirms the real potential of the proposed catalytic system. This catalyst was also used in the hydrogenation of levulinic acid to produce γ-valerolactone selectively.
The fast and the furfural: Furfuryl alcohol is produced from furfural with a yield of 88 % in the presence of a recyclable and stable Co/SBA-15 catalyst at 150 °C under H2 pressure in ethanol. This catalyst is also active and selective in the hydrogenation of levulinic acid to γ-valerolactone.