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Advanced Energy Materials

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Online ISSN: 1614-6840

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Print ISSN: 1614-6832

Disciplines: Materials science

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Schematic of the integrated device. a) Schematics of the integrated device for generating electricity and clean water simultaneously from the solar‐driven interfacial evaporation process. The device incorporates a flipping design to prevent salt crystal precipitation and activate the electrode. b) The hybrid electrode is composed of a solar absorbers layer, a current collector, and an electrode material layer. c) SEM image of PANI@GO/MnO2, the inset shows its corresponding HR‐TEM. d) XPS of Mn 3s doublet for PANI@GO/MnO2.
Power production performance of interfacial solar steam generation. a) Evaporation rate and the corresponding solar thermal efficiency under different solar irradiations. b) Mass change of water under different solar irradiations.
Salinity‐gradient energy harvested from the evaporation under solar irradiation. a) The Voc of the device over time under different solar irradiations, the inset is the photograph of integrated device under solar irradiation. b) The characteristic current‐voltage curves of integrated device under different solar irradiations. c) The output power of the device under different solar irradiations. d) The Voc of device over time under solar intensity of 1 kW m⁻² without flipping. e,f) Photographs of solar absorbers from the integrated device without flipping at the 1st cycle (e) and with flipping at the 121st cycle (f). g) The Voc of the device recorded for 121 cycles by periodically flipping the device (under the solar intensity of 1 kW m⁻²). (h) Power density and measured voltage/ theoretical voltage (VM/ VT) reported previously, in comparison with our results, referring to Table S1 (Supporting Information), for details.
The potentials developed at the electrode and across the separator from the salinity‐gradient under illumination. a) The schematic of the device describing the potentials developed from the electrode and the membrane. b) The Voc obtained by using PANI@GO/MnO2 electrode and carbon cloth electrode with different membranes under illumination of 2.0 kW m⁻².
Structure characterizations of the PANI@GO/MnO2 electrodes. a) Typical SEM image and TEM image b) of pristine PANI@GO/MnO2. (b1‐b4) TEM‐EDS elemental mappings for nitrogen (b1), oxygen (b2), sodium (b3), manganese (b4) of the pristine PANI@GO/MnO2. c,d) SEM image (c) and TEM image (d) of PANI@GO/MnO2 after discharge at the 1st cycle. (d1‐d4) TEM‐EDS elemental mappings for nitrogen (d1), oxygen (d2), sodium (d3), manganese (d4) of PANI@GO/MnO2 after discharge at the 1st cycle. (e‐g) XPS narrow scan spectra for PANI@GO/MnO2 at pristine state e), discharge state f) at the 1st cycle, and charge state g) at the 100th cycle.

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A High‐Efficiency System for Long‐Term Salinity‐Gradient Energy Harvesting and Simultaneous Solar Steam Generation

November 2024

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919 Reads

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Jun Yin

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Fuhua Yang

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Advanced Energy Materials, part of the prestigious Advanced portfolio, is your prime applied energy journal for research providing solutions to today’s global energy challenges. Your paper will make an impact in our journal which has been at the forefront of publishing research on all forms of energy harvesting, conversion and storage for more than a decade. The Advanced portfolio from Wiley is a family of globally respected, high-impact journals that disseminates the best science from well-established and emerging researchers so they can fulfill their mission and maximize the reach of their scientific discoveries.

Recent articles


Interaction mechanisms and film‐formation dynamics of MA‐free perovskite with TC additive. a) Schematic illustration of blade‐coating FA0.95Cs0.05PbI3 perovskite film with the additive TC. b) ¹H NMR spectra of neat FAI solution, neat TC solution, and the mixed solution of FAI and TC. c) ¹H NMR spectra of neat TC and the mixed solution of PbI2 and TC. d) The magnified FTIR spectra of neat TC, neat perovskite components, and their mixtures at different wavenumber regions. XPS spectra of e) N 1s and f) S 2p of TC and perovskite components. g) XPS spectra of Pb 4f of the control and target perovskite films. h) In situ PL spectrum of the control perovskite and target perovskites during the film‐formation process. i) Evolution of the maximum PL intensity for the control and the target perovskites during the film‐formation process.
Film quality of control and target perovskite layers by ambient blade‐coating. a) Top‐view and cross‐sectional SEM images. b) AFM height images. c) XRD patterns. d) UV–vis absorption spectra. The inset is the tauc plots. e) Steady‐state PL and f) TRPL spectra. g) PL mapping images.
Device performance of the control and target PSCs. a) J‐V curves of the optimal small area devices (0.09 cm²) under 1‐sun illumination. b) The stabilized power output (SPO) curves under 1‐sun illumination for 3600 s. c) EQE curves. d) J‐V curve of the optimal target device with an active area of 1 cm². e) Electrical impedance spectroscopy (EIS) plots. f) Dark I–V curves of electron‐only devices. The inset is the histogram of trap density (Nt). g) Evolution of PCEs for the control and target devices during thermal aging at 85 °C in a N2‐golve box. h) Evolution of PCEs for the control and target devices during long‐term storage in ambient conditions at 25 °C with a relative humidity of 25%. i) Comparison of the PCEs of the printed PSCs from different methods after long‐term storage in ambient conditions.
The long‐term stability of the ambient‐printed perovskite films. a) XRD patterns of the control and target perovskite films after annealing at 85 °C in N2 atmosphere for different times. b) SEM images of the control and target perovskite films after annealing at 85 °C in N2 atmosphere for 28 days. c) XRD patterns of the control and target perovskite films stored at 85% relative humidity for different times. d) SEM images of the control and target perovskite films stored at 85% relative humidity for 28 days. e) Proposed degradation mechanism of the control and target films during thermal aging and ambient storage.
Ambient‐Printed Methylammonium‐Free Perovskite Solar Cells Enabled by Multiple Molecular Interactions
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January 2025

Lei Lang

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Zicheng Ding

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Yachao Du

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Shengzhong (Frank) Liu

The ambient printing of high‐performance and stable perovskite solar cells (PSCs) is crucial for enabling low‐cost and energy‐efficient industrial fabrication. However, producing high‐quality perovskite films via ambient printing remains challenging due to direct exposure to air, which easily induces additional stacking defects and triggers perovskite degradation compared to films fabricated by traditional spin‐coating under inert conditions. Here, a multiple molecular interaction strategy is introduced to address this challenge by incorporating a 2‐thiazole formamidine hydrochloride (TC) additive, effectively suppressing defect formation during ambient printing. The specific interactions between TC and precursor components, i.e., multiple hydrogen bonds and coordination interactions, could promote the crystallization of α‐phase perovskites and reduce cation and anion vacancies simultaneously when drying in air. These endows high‐quality ambient‐printed perovskite films with large crystalline grains with eliminated nanovoids and low trap‐densities, which improve charge carrier dynamics and prevent perovskite decomposition and hydration under thermal/humidity stress during long‐term annealing/ambient storage. The unencapsulated PSCs show a high efficiency of 23.72% with good stability, i.e., realizing 92% and 95% efficiency retention after 672 h of annealing at 85 °C in a N2 atmosphere and after 2088 h of storage in ambient air.


Confining Surface Oxygen Redox in Double Perovskites for Enhanced Oxygen Evolution Reaction Activity and Stability

Natasha Hales

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Jinzhen Huang

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Benjamin Heckscher Sjølin

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Emiliana Fabbri

Nickel‐based double perovskites AA′BB′O6 are an underexplored class of oxygen evolution reaction (OER) catalysts, in which B‐site substitution is used to tune electronic and structural properties. BaSrNiWO6, with a B‐site comprised of alternating Ni and W, exhibits high oxygen evolution activity, attributed to the evolution of a highly OER active surface phase. The redox transformation of Ni²⁺(3d⁸) to Ni³⁺(3d⁷) combined with partial W dissolution into the electrolyte from the linear Ni(3d)‐O(2p)‐W(5d) chains drives an in situ reconstruction of the surface to an amorphized, NiO‐like layer, promoting oxygen redox in the OER mechanism. However, the high valence W⁶⁺(5d⁰) acts as a stabilizing electronic influence in the bulk, preventing the mobilization of lattice oxygen which is bound in highly covalent W─O bonds. It is proposed that the surface generated during the OER can support a lattice oxygen evolution mechanism (LOEM) in which oxygen vacancies are created and preferentially refilled by electrolytic OH⁻, while bulk O species remain stable. This surface LOEM (sLOEM) allows BaSrNiWO6 to retain structural integrity during OER catalysis. With a Tafel slope of 45 mV dec⁻¹ in 0.1 m KOH, BaSrNiWO6 illustrates the potential of Ni‐based double perovskites to offer both OER efficiency and bulk stability in alkaline electrolysis.


Impurity Impacts of Recycling NMC Cathodes

Zifei Meng

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Xiaotu Ma

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Jiahui Hou

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[...]

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Yan Wang

The skyrocketing demands for electric vehicles cause large quantities of spent lithium‐ion batteries (LIBs) and pressure on the global supply chain, leading to raw materials shortages and cost increases. In LIBs, LiNixMnyCozO2(NMC) cathodes are one of the major cathode materials. Thus, recycling NMC cathodes from spent lithium‐ion batteries is emerging because they contain abundant valuable materials, which can be considered unique “mineral” sources. Impurities are one of the main concerns for introducing recovered materials back into new battery manufacture because impurities are typically considered to impair the properties of recovered materials. However, some impurities can beneficially act as dopants or coatings. To comprehensively understand the effects of different impurities and treat impurities properly, this review summarizes the origin and species of possible impurities which can be introduced during different pretreatment processes, analyzes the methods to remove impurities, and discusses the effects of impurities on the regeneration process and recovered materials. This work also outlines future perspectives for fundamental research about impurities and relevant challenges of the recycling industry, helps academia and manufacturers to create new impurity standards of recovered cathode materials, and suggests opportunities for achieving a circular economy for the lithium‐ion batteries industry.


Preparation of surface‐functionalized metal foils. a) Schematic diagram of the preparation process for surface‐functionalized metal foils, where the metal foil is unrolled at a controllable speed into a reaction tank containing a strongly reducing liquid lithium source reagent. After an alloying reaction occurs, the functionalized current collector can be obtained through drying. b) Optical photographs (left) and SEM surface morphology characterization (right) of surface morphology of pure In foil and surface‐functionalized In foil. c) Cross‐sectional SEM image of the surface‐functionalized In foil and corresponding EDS elemental distribution mapping spectra of In and O (Li).
Controllable quantity of preloaded lithium. a) XRD patterns of each set of In@LiIn collectors after alloying pure In with a 0.5 mol L⁻¹ Li‐Naph/DME solution for different durations. b) The thickness of the Li‐In alloy layers in each set of In@LiIn collectors, obtained via cross‐sectional SEM after alloying pure In with a 0.5 mol L⁻¹ Li‐Naph/DME solution for varying durations. c) The electrochemical delithiation curves of each set of In@LiIn collectors after alloying pure In with a 0.5 mol L⁻¹ Li‐Naph/DME solution for varying durations. d) The electrochemical delithiation curves of each set of In@LiIn collectors after alloying pure In with Li‐Naph/DME solutions of different concentrations for 5 min.
Electrochemical performance of surface‐functionalized foil materials. a) Lithium nucleation overpotential comparison between In@LiIn collector and pure In collector. b) EIS spectra of In@LiIn collector and pure In after the first cycle in a half cell. c) After the first cycle, SEM images of In@LiIn and pure In surface morphology(left), and schematic diagrams of lithium plating processes (right). d) The stacked charge‐discharge curves of pure In and In@LiIn collectors at different cycle numbers with a fixed deposition capacity of 1 mAh cm⁻² and an delithiation cutoff voltage of 1.2 V. e) The cumulative lithium loss of the pure In and In@LiIn collectors from 2 to 50 cycles. The quantified difference value between the cumulative lithium loss of the pure In collector and the In@LiIn collector in each cycle is defined as the cumulative compensated lithium amount of the In@LiIn collector in actual cycling (marked by the arrow).
Electrochemical performance and mechanism of prestorage Li compensation. a) Cycling performance of the LFP||In@LiIn and LFP||pure In cells at 0.5C, along with SEM characterization of In@LiIn and pure In surface morphology after 25 cycles. b) First cycle charge and discharge curves of the LFP||In@LiIn and LFP||pure In cells. c) Schematic diagrams of the lithium stripping and platting processes in full cell.
Scalability of the surface‐functionalized alloying foil. a) Optical images and SEM images of pure In and In@LiIn collectors with mesh‐like 3D pattern structures. b) Optical images and SEM images of pure In and In@LiIn collectors with island‐like 3D pattern structures. c) SEM cross‐sectional views of island‐like pure In and In@LiIn collectors. d) Electrochemical delithiation curves of original, island and mesh In@LiIn collectors, which were obtained by alloying pattern‐designed pure In foil in a 0.5 mol L⁻¹ Li‐Naph/DME solution for 3 min. e) Surface morphology of In@LiIn collectors with island‐like 3D pattern structures after the lithium deposition of 1 mAh cm⁻². f) Surface morphology of island‐like In@LiIn collectors after 150 cycles. g) Alloying processes of various metal foils based on the redox potentials of Li‐Naph and Li‐MBP complexes. h) XRD patterns and optical photographs of Sn and Ga foils after alloying in Li‐Naph/DME solution.
Functional Alloy Collector Capable of Sustainable Lithium Compensation for Anode‐Free Batteries by a Controlled Lithium‐Prestorage Technology

Yao Liu

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Cheng Zeng

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Mingtao Hu

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[...]

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Huiqiao Li

With higher energy density and reduced cost, anode‐free battery has attracted great attention from both academic and industry. However, the development of anode‐free batteries is hindered by their poor cycle life due to the continuous irreversible lithium (Li) consumption at the anode side. Here, a surface‐functionalized alloy foil, which can gradually release active lithium to the cell upon cycling, used as the collector for anode‐free batteries is proposed. The alloy foil is prestored with a certain amount of active lithium via a simple wet contacting reaction between the metal foil and liquid lithium source reagent. The prestored lithium amount can be precisely controlled by reagent concentration and contact time. When the foil is used as the anode, its alloyed surface demonstrates a low nucleation barrier for lithium deposition and a more uniform deposition behavior. More importantly, the alloy collector can rationally release active lithium to sustainably compensate for the irreversible Li consumption upon the cycling of a full cell, thus greatly prolonging the cycle life of the anode‐free battery by 10 times. Besides, this technique can be extended to diverse metal collectors demonstrating its broad applicability.


Functionalized Interlayers in Self‐Powered Organic Photodiodes for Enhanced Near‐Infrared Sensing

Yongju Lee

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Swarup Biswas

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Dong Hyun Nam

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Hyeok Kim

There is a growing interest in fabricated organic material‐based photodiodes (OPDs) since they are lightweight, flexible, and cost‐effective to manufacture. Notably, they exhibit near‐infrared photo‐sensing capabilities that are self‐powered, a feature attributed to the tunable optical properties of organic semiconductor (OSC) materials. Nonetheless, the application of OPDs in the semiconductor industry encounters challenges compared to their inorganic counterparts, such as low sensitivity and limited durability. In this study, a self‐powered OPD using a poly[4,8‐bis(5‐(2‐ethylhexyl)thiophen‐2‐yl)benzo [1,2‐b:4,5‐b′]dithiophene‐2,6‐diyl‐alt‐(4‐(2‐ethylhexyl)‐3‐fluorothieno[3,4‐b]thiophene‐)‐2‐carboxylate‐2‐6‐diyl)]:biaxial active layer of phenyl‐C70‐butyric acid methyl ester (PTB7‐Th:PC70BM) and an organic hole transport layer (HTL) composed of poly(3,4‐ethylenedioxythiophene) and poly(styrene sulfonate) (PPY:PSS) is developed. These results highlight the effectiveness of PPY:PSS as an HTL, demonstrating distinct improvements in efficiency, photosensitivity, photo‐detectivity, and operational stability of the OPD when the weight ratio between the PPY and PSS is 1:2.


Mechanisms of Crystallization Regulation. A) Schematic diagram of three‐in‐one strategy. B) Optical images of the nucleation and crystal growth process of control, BB perovskite films. C) The SEM images of the buried interface from the bottom of control and BB perovskite films, scale bars, 500 nm. D) Schematic diagram of the nucleation and crystallization for control and AmiHCl‐treated perovskite films.
Characterization of Perovskite Film Quality. A) XRD patterns of the wet control and Bulk perovskite films without annealing. B) XRD patterns of perovskite films with various AmiHCl treatments after annealing. C) The XRD peak intensity ratio of (001)/(011) and (001)/PbI2 extracted from B). Grazing‐incident wide‐angle X‐ray scattering profiles of D) control and E) BB perovskite films with the angle of incident beam ranging from 0.2 to 1.2°. F) The qz values obtained from (001) plane as a function of incidence angle. G) The top view SEM images of control and BBT perovskite film, scale bars, 500 nm. H) The AFM images of control and BBT perovskite film, scale bars, 500 nm.
Carrier Dynamics in Perovskite Films. A) Pseudo‐color TA plots, B) transient absorption (signal excitation) spectra in the range of 0.086–24.3 ps, C) transient absorption (signal attenuation) spectra in the range of 24.3 ps‐1260 ps of the control perovskite film. D) Pseudo‐color TA plots, E) transient absorption (signal excitation) spectra in the range of 0.086–20.5 ps, F) transient absorption (signal attenuation) spectra in the range of 20.5–1260 ps of the BBT perovskite film.
Photovoltaic Performance of PSCs. A) Statistical box charts of VOC JSC, FF, and PCE were obtained from the control and BBT devices. B) J–V curves of the best‐performing control and BBT devices. C) EQE spectra and D) SPO efficiencies of the best‐performing control and BBT devices. E) J–V curves of large area (1 cm²) BBT devices.
Stability of Perovskite films and devices A) Photographs of control and BBT perovskite films aged in air with RH of 80%. B) PCE evolution of pristine encapsulated control and BBT devices under continuous MPP output in N2 atmosphere for 1350 h (ISOS‐L‐1).[⁵⁴] C) Stability test of encapsulated control and BBT devices stored under 85% humidity (65 °C) for 1000 h (ISOS‐D‐3).[⁵⁴]
Stable and Efficient Perovskite Photovoltaics via a Three‐In‐One Passivating Approach by Aminoacetonitrile Hydrochloride

Yinjiang Liu

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Tengfei Kong

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Yang Zhang

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[...]

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Dongqin Bi

Reducing defect density is of significant importance for enhancing the power conversion efficiency (PCE) and stability of perovskite solar cells (PSCs). While most previous outstanding studies have focused on individual layers within the perovskite device structure. Herein, a three‐in‐one strategy using the aminoacetonitrile hydrochloride (AmiHCl) molecule to reduce the defects in the bulk and surface of perovskite. The results of the study found that the AmiHCl bottom modification can decrease the number of buried interface holes, doping into bulk perovskite can modulate crystallization via a strong interaction between AmiHCl and perovskite components, and the upper interface modification can inhibit the formation of vacancies by creating hydrogen bonds with A‐site cations. This approach yields PSCs with an efficiency of 25.90% and a high fill factor (FF) of 88.54%. Additionally, the modified PSCs show significantly enhanced operational stability, with the PCE retaining more than 90.0% of the initial value after 1350 h of maximum power point tracking.


Host–Guest Complexation of α‐Cyclodextrin and Triiodide Ions for Enhanced Performance of Ionic Thermoelectric Capacitors

Shih‐Ting Kao

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Ching‐Chieh Hsu

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Shao‐Huan Hong

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[...]

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Cheng‐Liang Liu

Ionic thermoelectric materials have emerged as a promising avenue for harvesting low‐grade waste heat, with significant potential for applications in wearable electronics. This study introduces a novel design for ionic thermoelectric capacitors (ITECs) by incorporating host–guest complexation between α–cyclodextrin (α‐CD) and triiodide ions (I3⁻). The strong host–guest complexation between α‐CD and I3⁻ confines the diffusion of I3⁻ within the cylindrical cavities of α‐CD, as evidenced by UV–vis spectroscopy and ¹³C‐NMR analysis. This confinement enhances the ion mobility difference between I3⁻ and sodium ions, which in turn significantly boosts the ionic thermopower of the polyvinyl alcohol/α‐CD/NaI hydrogels. Accordingly, the optimized sample achieves an impressive positive ionic thermopower of 14.24 mV K⁻¹ and a high ionic power factor of 477.2 µW K⁻² m⁻¹. Furthermore, the stretchable ITEC demonstrates a substantial power density of 5.9 mW m⁻². When integrated into a 3‐leg device, a stable thermovoltage of 176 mV is generated under a temperature gradient of 4.4 K, thus highlighting the potential of this system for efficient thermal energy harvesting.


Room‐temperature carrier concentration versus mobility for A typical semiconductors and thermoelectrics[¹²] and B several CaAl2Si2‐type Zintl compounds[19,22–24] and (inset) half‐Heusler compounds.[¹²]
A) Schematic diagram of polar optical phonon scattering. B) Phonon dispersion and phonon density of states (DOS) values for CaMg2Sb2. C) Polar coupling constant for some semiconductors. Results for CaAl2Si2‐type Zintl compounds were calculated based on the parameters provided in Table S1 (Supporting Information) and those for other compounds are from previous reports.[12,13] D) Carrier mobility and carrier concentration values for Ca1‐x‐yLiyYbzMg2‐xCdxSb2. E Formation energy for Ca and Mg vacancies in Ca8Mg16Sb16, Ca8Mg12Cd4Sb16, and Ca6Yb2Mg12Cd4Sb16. F Temperature‐dependent carrier mobility for Ca1‐x‐yLiyYbzMg2‐xCdxSb2.
Temperature‐dependent A) electrical conductivity and B) Seebeck coefficient for Ca1‐x‐yLiyYbzMg2‐xCdxSb2. Carrier‐concentration‐dependent C) Seebeck coefficient and D) power factor for Ca1‐x‐yLiyYbzMg2‐xCdxSb2 at room temperature and corresponding calculated density‐of‐states effective mass values. E Electronic band structures for Ca8Mg16Sb16, Ca8Mg12Cd4Sb16, and Ca6Yb2Mg12Cd4Sb16. F) Calculated Fermi surfaces at the Fermi energy levels of −0.1 and −0.26 eV in the first Brillouin zone of Ca6Yb2Mg12Cd4Sb16.
A) Temperature‐dependent lattice thermal conductivity for Ca1‐x‐yLiyYbzMg2‐xCdxSb2. B) Phonon DOS for Ca8Mg16Sb16, Ca8Mg12Cd4Sb16, and Ca6Yb2Mg12Cd4Sb16. Phonon dispersions C) for Ca8Mg16Sb16 and Ca8Mg12Cd4Sb16 and D) for Ca8Mg12Cd4Sb16 and Ca6Yb2Mg12Cd4Sb16. E) phonon group velocity for Ca8Mg16Sb16, Ca8Mg12Cd4Sb16, and Ca6Yb2Mg12Cd4Sb16. F) Calculated electron localization function (ELF) for the (1 1 0) plane in Ca8Mg12Cd4Sb16 and in Ca6Yb2Mg12Cd4Sb16.
A) Temperature‐dependent ZT of Ca1‐x‐yLiyYbzMg2‐xCdxSb2; B) Comparison of temperature‐dependent ZT between this work and other exceptional CaMg2Sb2‐based and p‐type Mg3Sb2‐based TE materials.[18,23,34]
Strong Polar Optical Phonon Screening and Softening Enhance the Thermoelectric Performance of Zintl Compounds

Muchun Guo

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Ming Liu

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Donglin Yuan

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[...]

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Jiehe Sui

Ternary CaAl2Si2‐structure‐type Zintl compounds are promising p‐type counterparts to n‐type Mg3(Sb, Bi)2 for thermoelectric energy conversion. However, many of these p‐type Zintl compounds suffer from low carrier concentration and mobility, resulting in poor thermoelectric performance. Here, it is revealed that their ultralow mobility stems from strong polar optical phonon scattering, and demonstrate that their electrical transport properties can be dramatically boosted by employing a screening effect. By employing isovalent alloying with Cd and Yb, along with Li aliovalent acceptor doping in CaMg2Sb2 to increase carrier concentration and induce a strong screening effect, a significant improvement in carrier mobility and, consequently, the power factor is achieved. Moreover, isovalent alloying weakens chemical bonding, causing the softening and deceleration of both acoustic and optical phonons and, thus, a reduction in lattice thermal conductivity. As a result, a ZT of 1.1 is achieved in the Ca0.69Yb0.3Li0.01Mg1.5Cd0.5Sb2 sample at 773 K, representing a 30‐fold increase compared to the pristine CaMg2Sb2. It is also proposed that the polar coupling constant can serve as a criterion for identifying materials with low intrinsic carrier concentration and mobility but with potential for thermoelectric applications facilitating the development of other thermoelectric materials beyond CaAl2Si2‐structure‐type Zintl compounds.


Photothermal Catalysts, Light and Heat Management: From Materials Design to Performance Evaluation

Enrique V. Ramos‐Fernandez

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Alejandra Rendon‐Patiño

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Diego Mateo

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[...]

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Jorge Gascon

Photothermal catalysis, a frontier in heterogeneous catalysis, combines light‐driven and thermally enhanced chemical reactions to optimize energy use and reaction efficiencies at catalytic active sites. By leveraging photothermal conversion, this approach links renewable energy sources with industrial chemical processes, offering significant potential for sustainable applications. This review categorizes photothermal catalysis into three types: light‐driven thermocatalysis, thermally enhanced photocatalysis, and photo‐thermo coupling catalysis. Each category is analyzed, emphasizing mechanisms, performance factors, and the role of advanced materials such as plasmonic nanoparticles, semiconductors, and hybrid composites in enhancing light absorption, thermal distribution, and catalytic stability. Key challenges include achieving uniform thermal and photonic energy distributions within catalytic reactors and developing accurate performance evaluation metrics. Applications such as CO₂ reduction, ammonia synthesis, and plastic upcycling highlight the environmental and industrial relevance of this technology. The review identifies limitations and suggests innovations in materials design and energy‐storing mechanisms to enable continuous catalytic processes. Future directions emphasize photothermal catalysis's potential to transform sustainable energy systems and advance green chemical production. This synthesis aims to guide research and foster practical adoption of photothermal technologies at an industrial scale.


Concurrent Operando Neutron Imaging and Diffraction Analysis Revealing Spatial Lithiation Phase Evolution in an Ultra‐Thick Graphite Electrode

Markus Strobl

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Monica E. Baur

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Stavros Samothrakitis

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[...]

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Yair Ein‐Eli

Energy‐efficient, safe, and reliable Li‐ion batteries (LIBs) are required for a wide range of applications. The introduction of ultra‐thick graphite anodes, desired for high energy densities, meets limitations in internal electrode transport properties, leading to detrimental consequences. Yet, there is a lack of experimental tools capable of providing a complete view of local processes. Here, a multi‐modal operando measurement approach is introduced, enabling quantitative spatio‐temporal observations of Li concentrations and intercalation phases in ultra‐thick graphite electrodes. Neutron imaging and diffraction concurrently provide correlated multiscale information from the scale of the cell down to the crystallographic scale. In particular, the evolving formation of the solid electrolyte interphase (SEI), observation of gradients in total lithium content, as well as in the formation of ordered LixC6 phases and trapped lithium are mapped throughout the first charge–discharge cycle of the cell. Different lithiation stages co‐exist during charging and discharging; delayed lithiation and delithiation processes are observed in central regions of the electrode, while the SEI formation, potential plating, and dead lithium are predominantly found closer to the interface with the separator. The study emphasizes the potential to investigate Li‐ion diffusion and the kinetics of lithiation phase formation in thick electrodes.




The state‐of‐the‐art battery energy metrics and the present industrial scenario for electric vehicles and other applications. a) The proposed battery demand in GWh for electronic devices (EDs), stationary storage (SS), and electric vehicles (EVs) up to the year 2030. b) The predicted metal‐air battery demands (USD Million) by 2030. c) Cell‐pack energy and driving range of commercial EVs (left) and the future energy (right) showing projected driving range with Tesla Model 3 Long range using ZABs pack‐energies of 85, 130, 220, and 400 kWh.[3a,c] d) Ragone plots for the carbon emissions, environmental impacts, safety risks, economic values, and resource contents for using 1 kg of Na‐ion, Li‐ion, and Zn‐air batteries. The safety risk is estimated for EUCAR standards. EUCAR is the European Council for Automotive R&D. e) Storage technology requirements for EDs, EVs, and (eVTOLs) and obtained ZABs performance metrics. f) Calculated power‐to‐energy ratio for 85 and 220 kWh for LIBs and ZABs using vehicle dynamics model with Urban Dynamometer Driving Schedule (UDDS) driving cycles.[⁴] Please see methods for details.
Mechanistic illustrations for designing high‐performance cathode and solid electrolytes. a) Comparison of bifunctional activity versus ORR half‐wave potentials. b) Radar charts grading the performance metrics for bifunctional catalysts. c) Structural influences for active electrochemical surface areas beyond the electrode‐electrolyte interphases (left). Electrochemical‐chemical kinetics (E‐C’) with insertion of intermediate reactants by transferring both the electrons and ions across the interface (middle). Kinetics for distribution of electrons for catalysts structure (right). The thermodynamic‐electrochemical driving force and electrical conductivity depend significantly on the position of the Fermi level. d) Comparison of the anion‐exchange membranes (AEMs), gel‐polymer electrolytes (GPEs), and solid‐polymer electrolytes (SPEs) based on the recently reported champion data. e) Radar chart for electrolyte performance metrics. f) Anion‐motifs‐related structures for SEs. TEMPO and O‐motifs (top, left), F ‐motif (top, right), S‐motif (bottom, left), quaternary and N‐motifs (bottom, right).
Illustration of designing Zn‐anodes and cell performance metrics for flexible ZABs. a) Ragone plot of areal capacity versus current density for different types of Zn‐anodes for symmetric cells. b) Radar chart for key performance metrics. c) Electrochemical challenges and rational design strategies for high‐performance Zn‐anodes with anion motifs employing the uniform current distribution, in situ formation of SEI, and anion fixation along with solid/liquid electrolytes. d) Evans diagrams for electrochemical kinetics of Zn‐anodes. Reproduced with permission.[3c] Copyright 2023, Wiley. e) Comparison of mechanical bending cycles with current density for flexible ZABs for planar (cyan region), wire (red region), fiber (blue region), and sandwich(magenta region) configurations. f) Ragone plots for comparison of performance metrics in flexible ZABs. g–h) Photographs of homemade (g), coin cells (h), and pouch cells (i) and their key distinctive parameters.
Illustration of key structural parameters for design of cathodes, electrolytes, anodes, separators, binders, and cell manufacturing for solid‐state ZABs.
Schematics displaying the cell manufacturing, processing, and cost analysis for solid‐state ZABs. a) The fabrication of cathode‐electrolyte electrodes includes a continuous slurry coating of the thin carbon layer and cathode materials (including active materials, binder, and carbon black) on the gas‐diffusion layer (GDL), calendaring, drying, and densification; then, follows the stacking of solid electrolytes/separators. b) Winding/cylindrical rolling of Zn‐anode and cathode‐electrolyte electrodes with laminating the air‐permeable layers. c) Z‐stacking of Zn‐anode sandwiched between cathode and solid electrolyte (SE) electrodes in parallel configurations. d) Assembly of ZABs includes winded electrodes and packaging in the cylindrical/prismatic cells. e) Assembly of ZABs includes parallel Z‐stacking and packaging in the pouch cells. f) Schematic of cell design under symmetric configurations. g) Projected LIBs, lithium‐sulfur (LiS), and ZABs battery pack‐level costs with driving range for EVs. Solid and dotted lines denote the probable span of driving range and battery pack cost. Reproduced with permission.[3c] Copyright 2023, Wiley.
Design Strategies for Practical Zinc‐Air Batteries Toward Electric Vehicles and beyond

Sambhaji S. Shinde

·

Sung‐Hae Kim

·

Nayantara K. Wagh

·

Jung‐Ho Lee

Zinc‐air batteries (ZABs) offer promising forthcoming large‐scale high‐density storage systems and the cost‐effectiveness of electrode materials, specifically in solid‐state and liquid electrolytes. However, the uncontrolled diffusion and utilization of irreversible zinc components and cell design principles limit practical applications with severe capacity fade and interfacial reactions. In this perspective article, the aim is to shed lights on the underlying mechanisms of solid electrolytes and interfaces alongside the current status and prospective research insights. Formulations of ampere‐hour (Ah)‐scale cylindrical/pouch cells are discussed for 100–500 Wh kg⁻¹ cell‐level energy metrics under realistic operations. The electrode/electrolyte interface dynamics, scale‐up readiness, testing protocols, and key performance metrics are also suggested for transforming lab‐scale research into practical production.


The in situ high‐temperature XRD patterns of a) the precursor without lithium salt, b) The mixture of precursor and LiOH·H2O. c) The schematic diagram of phase transition during calcination process of the precursor‐LiOH·H2O mixture. R, M, and S refer to the rhombohedral, monoclinic, and spinel phase, respectively.
The in situ high‐temperature Raman spectra of the mixture of precursor and LiOH·H2O. a) The overall phase transition process. b) The TM3O4→LixTM1‐xTM2O4 transition. c) The LixTM1‐xTM2O4→LiTMO2 transition. d) The LiTMO2→Li2TMO3 transition.
The ex situ high‐temperature structural evolution of precursor‐LiOH·H2O mixture. a) The ex situ XRD plots from 400 to 900 °C. b) Temperature dependent curves of the phase proportion obtained from XRD refinement. c) The interlayer Li/TM mixing and d) the FWHM of (020) peak versus temperature curves. The normalized XANES spectra of the samples quenched on 500 and 800 °C at e) Ni K‐edge and f) Mn K‐edge. The EXAFS spectra of the samples at g) Ni K‐edge and h) Mn K‐edge. i) The schematic diagram of phase transition from LiTMO2 (R3¯${\bar{3}}$m) to Li2TMO3 (C2/m).
The in situ high‐temperature XRD patterns of pre‐heated precursor‐LiOH·H2O mixture during 120 min holding at a) 750 °C, b) 800 °C, c) 850 °C, and d) 900 °C. The alteration in the phase ratio of LiTMO2 and Li2TMO3 in relation to reaction time at e) 750 °C, f) 800 °C, g) 850 °C, and h) 900 °C. i) The evolution of the fitted k value as a function of temperature. j) Plots of lnk against 1/T to ascertain the Arrhenius activation energy of phase transition from LiTMO2 (R3¯${\bar{3}}$m) to Li2TMO3 (C2/m). k) The schematic illustration of LiTMO2‐Li2TMO3 phase evolution from 750 to 900 °C.
The structure and electrochemical performance of the pristine sample. a) The XRD refinement pattern and b) the Raman pattern of the pristine. The AC‐STEM images accompanied with the corresponding Fast Fourier Transform (FFT) and the line intensity in the selected region of the pristine along c) [110]M axis and d) [110]R axis. e) The initial charge and discharge curves of the pristine at 0.1 C (1 C = 250 mAh g⁻¹). f) The discharge capacity and energy density of the pristine during cycling at 1 C.
Phase Transition Behavior During Sintering Process of Li‐Rich Materials

Mengke Zhang

·

Jiayang Li

·

Qi Pang

·

[...]

·

Xiaodong Guo

Phase transition serves as an ordinary behavior occurring during the high‐temperature calcination process, while it becomes quite complicated in Li‐rich materials composed of rhombohedral phase LiTMO2 (TM: Ni, Mn) with R3¯3ˉ{\bar{3}}m space group and monoclinic phase Li2TMO3 with C2/m space group. Yet to be firmly elucidated is how the precursor transforms into LiTMO2 (R3¯3ˉ{\bar{3}}m)‐Li2TMO3 (C2/m) compound and what is the precise conversion mechanism between these two phases. This work systematically elaborates the structural evolution with Li/O incorporation during calcination, and proposes a LiTMO2 to Li2TMO3 phase transition mechanism. A series of characterizations on structural rearrangement and detailed analysis provide insights into the comprehension of this transition, i.e., the transition metal (TM) vacancies induced by interlayer TM ions migration function as the primary reason driving the transformation from LiTMO2 to Li2TMO3. This work offers a novel concept for the structural regulation in Li‐rich cathodes.




Schematics of the solvation structures, interfacial reaction mechanisms, and Na deposition morphology in the conventional electrolytes, WSEs and the DWIEs.
The solvation structure of DWIEs. a) Schematic of interactions among Na⁺, FSI⁻, THF, and DBE within 1‐T/B electrolyte. b,c) FTIR spectra of THF, DBE, and THF/DBE (1:1 by vol) mixed solvents. d) Raman spectra of 1‐T, 1.86‐T, and 1‐T/B electrolytes and corresponding solvents. e) Fitting data of Raman spectra of different electrolytes at NaFSI regions. f) The proportion of SSIPs, CIPs, and AGGs in different electrolytes.
Compatibility of 1‐T, 1.86‐T, and 1‐T/B electrolytes with sodium‐metal anode. a) CEs of Na||Cu cells by the modified Aurbach method. b) CEs of Na||Cu cells at a current density of 0.2 mA cm⁻² for 0.2 mAh cm⁻². c) Cycling performance of Na||Na cells at a current density of 1 mA cm⁻² for 1 mAh cm⁻². SEM images of deposited Na on Cu foil in the d) 1.86‐T and e) 1‐T/B electrolytes. C 1s, O 1s, and F 1s XPS spectra of deposited Na on Cu foil in 1.86‐T (f) and 1‐T/B (g) electrolytes (first cycle deposition at 0.2 mA cm⁻² for 2.0 mAh cm⁻²). The elemental composition and their proportion of SEI formed in (h) 1.86‐T and (i) 1‐T/B electrolytes.
Regulation of dual‐weak‐interaction effects. a) ESP of of DBE and DBEi. b) FTIR spectra of THF/DBE and THF/DBEi mixed solvents (1:1 by vol). The RDF profile of c) 1‐T/Bi and d) 1‐T/B electrolytes. e) CEs of Na||Cu cells by the modified Aurbach method at a current density of 0.4 mA cm⁻². f) Long‐term cycling and CEs of Na||Cu cells at a current density of 0.2 for 0.2 mAh cm⁻².
Electrochemical performance of NVP||Na cells with different electrolytes. a) The charge‐discharge curves of NVP||Na cells toward different electrolytes. b) Cycling performance of high‐loading NVP (8.8 mg cm⁻²) ||Na (50 µm) full‐cells with different electrolytes at 1C. c) Long‐term cycling performance of NVP||Na cell with different electrolytes at 5C. d) A summary of CEs for Na||Cu cells tested using the Aurbach method based on electrolyte design. More details are given in Table S2 (Supporting Information).[31–41] e) Comparison of the enhancement in cycling performance of NVP||Na full‐cells and CE of Na||Cu cells achieved by solvation structure optimization.
Modulating Double‐Layer Solvation Structure via Dual‐Weak‐Interaction for Stable Sodium‐Metal Batteries

Sodium‐metal batteries are the most promising low‐cost and high‐energy‐density new energy storage technology. However, the sodium‐metal anode has poor reversibility, which can be optimized by constructing the robust solid electrolyte interphase (SEI). Here, a concept of dual‐weak‐interaction electrolyte (DWIE) is demonstrated, its double‐layer solvation structure is composed of weakly solvated tetrahydrofuran as the inner layer, and dipole interaction are introduced in the outer layer by dibutyl ether. This double‐layer solvation structure dominated by contact ion pairs and aggregates can promote to deriving of inorganic‐rich SEI film, resulting in smooth and dendrite‐free sodium‐metal deposition. By adjusting the molecular configuration of dibutyl ether to diisobutyl ether, the dipole interaction is further enhanced, resulting in stronger weakly solvating effect. Thus, the Na||Cu cells using the optimized DWIE achieved a high Coulombic efficiency of 99.22%, surpassing most electrolyte design strategies. Meanwhile, at 5C, the Na3V2(PO4)3 (NVP)||Na cell achieves stable cycling exceeding 3000 cycles. Even under rigorous conditions of ≈8.8 mg cm⁻² NVP loading and 50 µm thickness Na, the full cell can achieve a long cycling lifespan of 217 cycles. The pioneering concept paves the way for crafting readily achievable, cost‐effective, and eco‐friendly electrolytes tailored for SMBs, and offers potential applications in other battery systems.


Conversion–Lithiophilicity Hosts Toward Long‐Term and High‐Energy‐Density Lithium Metal Batteries

Lithium metal anode emerges as an ideal candidate for the next generation of high‐energy‐density batteries. However, challenges persist in achieving high lithium utilization rates while maintaining the demands of high energy density and extended cycle life. In this work, a novel conversion–lithiophilicity strategy is proposed to regulate the longevity of high‐energy‐density batteries by injecting lithium ion activity. This strategy is validated through carbon nanofiber decorated with Fe3C and Fe2O3 particles. The uniform metallic lithium deposition induced by lithiophilic Fe3C substrates has been verified through lithium deposition/stripping experiments and density functional theory calculations. The electrochemical active Fe2O3 component supplies additional anodic capacity and suppress battery degradation, as demonstrated in lithium‐ion storage research and three electrode system studies. When paired with LiFePO4 cathodes at an N/P ratio of 2, the full battery showcases outstanding cycling stability over 300 cycles at 1C, with an exceptional energy density of 438 Wh kg⁻¹ (calculated based on the cathode material and lithium content). Furthermore, the full battery delivers rapid kinetics of 124 mAh g⁻¹ at 2C. The conversion–lithiophilicity strategy presented offers a promising avenue for the development of high‐energy density and long‐life lithium metal batteries.


Cu‐Driven Active Cu2Se@MXene Heterointerface Reconstruction and Co Electron Reservoir Toward Superior Sodium Storage

Heterostructure engineering and active component reconstruction are effective strategies for efficient and rapid charge storage in advanced sodium‐ion batteries (SIBs). Herein, sandwich‐type CoSe2@MXene composites are used as a model to reconstruct new active Cu2Se@MXene heterostructures by in situ electrochemical driving. The MXene core provides interconnected pathways for electron and ion conduction, while also buffering volumetric expansion to stabilize the structure. This reconstructed Cu2Se@MXene heterointerface features abundant sodium storage active sites, enhanced Na⁺ adsorption, and diffusion kinetics, thus increasing sodium storage capacity. Moreover, the elevated Co valence state during the discharge process allows it to act as an electron reservoir to provide additional electron supply for Cu2Se conversion and accelerate the sodium storage kinetics. When employed as an anode in SIBs, the CoSe2@MXene electrode exhibits high capacity (694 mAh g⁻¹ at 0.1 A g⁻¹), excellent rate performance (425 mAh g⁻¹ at 20 A g⁻¹), and exceptional durability (437 mAh g⁻¹ after 10 000 cycles at 5 A g⁻¹ with a 0.0014% capacity decay per cycle). The electrochemical reconstruction and sodium storage mechanism of Cu2Se@MXene anode is further revealed through ex situ characterization and theoretical calculations. This work provides a new approach for designing advanced conversion‐type anodes for SIBs.


a) The synthesis of EBBT‐COF and PBBT‐COF. The simulated AA stacking of b,c) EBBT‐COF and d,e) PBBT‐COF. f) PXRD, g) N2 sorption isotherms, h) SEM image, and i) HR‐TEM image of EBBT‐COF. j) PXRD, k) N2 sorption isotherms, l) SEM image, and m) HR‐TEM image of PBBT‐COF.
a) UV–vis DRS spectra of EBBT‐COF and PBBT‐COF. b) Tauc plots of EBBT‐COF and PBBT‐COF. c) Bandgap structure diagram of EBBT‐COF and PBBT‐COF. d) Transient photocurrents of EBBT‐COF and PBBT‐COF. e) H2O2 yield of EBBT‐COF and PBBT‐COF. f) AQY of EBBT‐COF. g) Comparison of SCC efficiency and H2O2 yield for EBBT‐COF with COF‐based photocatalysts reported thus far. h) H2O2 yield of EBBT‐COF and PBBT‐COF in the five successive cycles of photocatalytic reactions.
a) The ORR polarization curves and Koutecky–Levich plots obtained by RDE measurements. b) RRED measurements of EBBT‐COF and PBBT‐COF. c) H2O2 selectivity and n of EBBT‐COF and PBBT‐COF. WOR polarization curves with a potential of d) +0.60 V versus Ag/AgCl and e) −0.23 V versus Ag/AgCl applied on Pt ring electrode. f) EPR trapping experiments for ·O2⁻ on EBBT‐COF and PBBT‐COF by DMPO in the dark and illumination for 10 min. g) Photocatalytic yield of ROS for EBBT‐COF and PBBT‐COF. h) In situ DRIFTS spectra for the photocatalytic system of EBBT‐COF.
a) The materials/electrons flowing pathway according to theoretical calculation. The numbers in circles are corresponding to the reaction Equations in the text (i.e., ① means Equation (1)) b) Gibbs free energy evolution during the reaction process. c) The π‐linking strength of the bond between the central and peripheral benzene rings in EBBT‐COF and PBBT‐COF.
Ethynyl‐Linked Donor–Acceptor Covalent Organic Framework for Highly Efficient Photocatalytic H2O2 Production

Photocatalytic H2O2 synthesis from H2O and O2 is considered to be one of the most promising alternative approaches for manufacturing H2O2. Developing highly active and selective photocatalysts is of significant in achieving efficient H2O2 photosynthesis. Herein, an ethynyl‐linked donor–acceptor covalent organic framework (COF), named EBBT‐COF, is prepared from the condensation reaction between an electron‐deficient unit 4,4′,4″‐(1,3,5‐benzenetriyltri‐2,1‐ethynediyl)tris‐benzenamine and an electron‐rich unit benzo[1,2‐b:3,4‐b′:5,6‐b″]trithiophene‐2,5,8‐tricarboxaldehyde. Powder X‐ray diffraction and N2 adsorption isotherm unveil the crystalline porous hcb network of EBBT‐COF with pores size centered at ca. 2.3 nm. Spectroscopic characterizations demonstrate the excellent visible‐light absorption capacity and enhanced photo‐induced charge separation and transport efficiency of EBBT‐COF owing to its donor–acceptor architecture. Density functional theory calculations and electrochemical tests indicate the high activity and selectivity of EBBT‐COF toward 2e⁻ O2 reduction reaction and 2e⁻ water oxidation reaction with triethynylbenzene and trithiophene moieties to accelerate O2‐to‐H2O2 and H2O‐to‐H2O2 conversion, respectively. These merits enable EBBT‐COF to be a promising photocatalyst toward H2O2 generation from H2O and O2 with a H2O2 yield rate of 5 686 µmol g⁻¹ h⁻¹, an optimal apparent quantum yield of 15.14%, a solar‐to‐chemical conversion efficiency of 1.17% (λ > 400 nm), representing one of the best performance among COF‐based photocatalysts reported thus far.


Functionalization of acceptor and donor AgBiS2 nanocrystal (NC) inks via ligand modulation. a) Schematic illustration of the solution‐phase ligand exchange (SPLE) and post‐treatment process of thiol group ligands for functionalizing acceptor and donor NCs. b) Band alignment diagram of [AgI2]⁻‐capped AgBiS2 NCs (acceptor) and further thiol group‐passivated AgBiS2 NCs (donor). c) FT‐IR spectra of 2‐mercaptoethanol, [AgI2]⁻‐capped AgBiS2 NCs, 2‐mercaptoethanol (2ME) treated [AgI2]⁻ capped AgBiS2 and oleate AgBiS2. d) Two‐dimensional Kelvin probe force microscopy (KPFM) potential image of the donor/acceptor stacked NC films. e) Molecular structure of bifunctional molecules and photographs showing the dispersibility of AgBiS2 NCs post‐treated with bifunctional molecules dispersed in N,N’‐dimethylformamide (DMF) solution.
Colloidal stability of donor and acceptor (D/A) AgBiS2 nanocrystal (NC) inks and the morphological properties of D/A‐blended AgBiS2 NC films fabricated from these inks. a) Colloidal stability of acceptor‐only ink and D/A‐blended ink prepared with different vol% of 2‐mercaptoethanol (2ME) (the right schematic image shows hydrogen bonding between 2ME and N,N’‐dimethylformamide ((DMF). b) Zeta potential of acceptor ink and donor NC ink prepared with different vol% of 2ME. c) Photographs of AgBiS2 NC films at varying NC ink concentrations. d) Thickness of AgBiS2 NC films according to NC ink concentration, estimated from cross‐sectional scanning electron microscope (SEM) images shown in Figure S9 (Supporting Information). e–g) Top‐view SEM images of acceptor, donor, and D/A‐blended films spin‐coated with a 250 mg mL⁻¹ ink concentration.
Photoinduced carrier dynamics in the active layers. a) Two‐dimensional transient absorption (TA) map of the acceptor film upon photoexcitation at 480 nm. b) Lifetime‐associated spectra of the acceptor film according to the global lifetime analysis. Global lifetimes are given in the panel. c) Schematic energy diagram depicting carrier relaxation and recombination pathways and associated timescales when the donor and acceptor films are photoexcited. d) Kinetic profiles of the donor (blue), acceptor (red), and D/A‐blended (purple) films probed at 1100 nm. Fit parameters are presented in Table S3 (Supporting Information).
Charge transfer and diffusion length characteristics in D/A‐blended AgBiS2 films. a) Illustration of the band diagram at the donor–acceptor nanocrystal (NC) interface. Photogenerated electrons and holes in the D/A‐blended films are extracted toward the acceptor and donor NCs, respectively, driven by the potential difference at the interface. b) Bar graph showing diffusion lengths calculated from the fitted values of the equivalent circuit in electrochemical impedance spectroscopy (EIS) for donor, acceptor, and D/A‐blended junction devices. c) Normalized transient photocurrent (TPC), d) normalized transient photovoltage (TPV), and e) open‐circuit voltage (Voc) as a function of light intensity for single and D/A‐blended junction devices. f) JSC graph of donor, acceptor, and D/A‐blended junction devices as a function of AgBiS2 film thickness plotted with the average for the three devices.
Photovoltaic performance of devices employing D/A‐blended AgBiS2 films. a) Cross‐sectional TEM image of the D/A‐blended junction solar cell, showing a thicker active layer compared to the conventional AgBiS2 single junction device. b) J–V curves of the optimized single junction and D/A‐blended junction solar cells. c) External quantum efficiency (EQE) and integrated JSC, and d) internal quantum efficiency (IQE) of the single junction and D/A‐blended junction devices at optimal thickness. e) Maximum power point tracking (MPPT) test for the single junction and D/A‐blended junction devices at ambient air and room temperature.
Homogeneously Blended Donor and Acceptor AgBiS2 Nanocrystal Inks Enable High‐Performance Eco‐Friendly Solar Cells with Enhanced Carrier Diffusion Length

Colloidal semiconductor nanocrystals (NCs) have garnered significant attention as promising photovoltaic materials due to their tunable optoelectronic properties enabled by surface chemistry. Among them, AgBiS2 NCs stand out as an attractive candidate for solar cell applications due to their environmentally friendly composition, high absorption coefficients, and low‐temperature processability. However, AgBiS2 NC photovoltaics generally exhibit lower power conversion efficiency (PCE) compared to other NC‐based devices, primarily due to numerous surface traps that serve as recombination sites, leading to a short diffusion length for free carriers. To address this challenge, this work develops donor and acceptor blended (D/A) AgBiS2 films. Through ligand modulation, this work formulates acceptor and donor AgBiS2 NC inks with suitable electrical band alignment for charge separation, while ensuring that they are fully miscible in the same solvent. This enabled the fabrication of high‐quality, thickness‐controllable D/A‐blended junction films. This work finds that this approach effectively facilitates carrier separation, leading to an enhanced carrier lifetime and diffusion length. As a result, using this approach, this work achieves AgBiS2 films that are twice as thick in solar cell applications compared to conventional devices, leading to improvements in current density and a solar cell PCE of 8.26%.


a) The solvent molecules (EG) can function as effective stabilizers of sulfur vacancies thus significantly increasing the electron concentration (n). b) The interfacial thermal resistance (Rk) introduced by the carbonization of solvent molecules can effectively suppress phonon propagation and further reduce κlat. c) Fewer defects and significantly decreased deformation potential (Edef) allow solvent doping can achieve higher carrier mobility (μ) than conventional solute doping. d) The comparisons between the temperature‐dependent ZT values of the solvent‐doped EG‐Bi2S3 sample in this work and several state‐of‐the‐art Bi2S3 materials.[⁷] e) The comparisons between the peak ZT and the average ZT value of the solvent‐doped EG‐Bi2S3 sample in this work and several state‐of‐the‐art Bi2S3 materials.[⁷]
Structural characterizations for EG‐Bi2S3 and Water‐Bi2S3 samples. a) Bi 4f and S 2p XPS spectra for Water‐Bi2S3 and EG‐Bi2S3 samples. b) The CDBS curves (ratio to Ni) of Water‐Bi2S3 and EG‐Bi2S3 samples, and the inset is the S parameter reflecting changes in defect concentration. c) C 1s XPS spectra for the SPSed EG‐Bi2S3 sample. d) C K‐edge XANES spectrum of the SPSed EG‐Bi2S3 sample.
Microstructure analysis for EG‐Bi2S3 sample. a) AC‐HRTEM image. b) The magnified image for the dashed box area in (a) clearly shows the presence of S vacancy. c) The IFFT image shows a high density of dislocations. d) Back‐scattered electron (BSE) images and corresponding elemental mapping for the SPSed EG‐Bi2S3 sample. e) High‐resolution TEM image of the SPSed EG‐Bi2S3 sample, clearly showing the presence of carbon. f) Representative AC‐HRTEM image and corresponding GPA strain map for Water‐Bi2S3 and EG‐Bi2S3 samples. g) X‐ray PDF data of Water‐Bi2S3, EG‐Bi2S3, and standard Bi2S3. h) Fitting of the experimental X‐ray PDF data in the r = 2–20 Å range for the EG‐Bi2S3 sample.
Electrical transport properties of the Water‐Bi2S3, EG‐Bi2S3 samples, and commercial Bi2S3, in which the data of undoped Bi2S3 synthesized with three different methods (melting, ball milling, and hydrothermal) are cited for comparisons.[7a,b,24] a) The Seebeck coefficient. b) The electrical conductivity. c) The DFT‐calculated deformation potentials (Edef) for conduction band for Bi24S36, Bi24S35, and Bi24S35‐EG supercell. d) The comparisons of electron scattering rate among Bi24S36, Bi24S35, and Bi24S35‐EG. e) The comparisons of Hall electron concentration (n) and mobility (μ) at 300 K between samples in this work and conventional‐doped Bi2S3 in references.[7c,d,8,26,32] f) The comparisons of the power factor (PF) values between the EG‐Bi2S3 sample in this study and several state‐of‐the‐art Bi2S3 samples obtained by conventional aliovalent doping.[7a,b,d,8,26]
Thermal transport properties and ZT values. The data of undoped Bi2S3 synthesized with three different methods (melting, ball milling, and hydrothermal) are cited for comparisons.[7a,b,24] a) Total thermal conductivity κt. b) Lattice thermal conductivity κlat and correspondingly simulated results of the EG‐Bi2S3 sample. c) The mismatch in phonon density of states between Bi2S3 and different forms of carbon. d) The temperature‐dependent ZT values of EG‐Bi2S3, Water‐Bi2S3, and common n‐type thermoelectric sulfides.[³⁴] e) The schematic diagram of our fabricated single‐leg TE module. f) The thermoelectric conversion efficiency (η) as a function of current (I) at different temperature differences (ΔT). The inset is the comparison between the η of the TE module in this work and other reported sulfide single‐leg TE modules.[7d,35]
Unconventional Solvent‐Doping‐Induced Ultrahigh Carrier Mobility Leads to Excellent Thermoelectric Performance in Eco‐Friendly Bi2S3 and SnS

Conventional aliovalent doping, which involves replacing host atoms with solute ones, is a well‐established strategy in wet chemical synthesis for enhancing semiconductor performance. However, this method faces serious challenges like low solubility and unavoidable carrier mobility loss, which hinder significant performance improvements, particularly in thermoelectrics. Herein, a novel solvent‐doping strategy is reported that effectively improves the carrier concentration in nanocrystals by stabilizing cation or anion vacancies. Density functional theory calculations and pair distribution function tests reveal that solvent doping increases the atomic ordering and reduces deformation potential, thereby significantly enhancing carrier mobility. Additionally, the conversion of solvent molecules into carbon contributes to further suppressing the lattice thermal conductivity in substrates. As a result, a record‐high peak ZT value of ≈1.0 and a measured thermoelectric conversion efficiency of 1.47% are obtained in solvent‐doped Bi2S3. Similarly, SnS exhibits a remarkable increase of ≈150% in the peak ZT value following solvent doping. This study demonstrates the application of solvent‐doping strategy in thermoelectrics and suggests the potential in other fields, such as transistors, photovoltaic, and catalysis.


Structure, principle, and electrical output characteristic of topological defect gyro‐multigrid triboelectric nanogenerator (TD‐GM‐TENG). a) Structure exploded diagram of TD‐GM‐TENG. b) Potential distribution simulation of TD‐GM‐TENG by COMSOL soft. c) Working principle of TD‐GM‐TENG. d) Physical photo of TD‐GM‐TENG. e) Operating principal diagram of TD‐GM‐TENG. f) Electrical output characteristic of TD‐GM‐TENG. g) Schematic diagram of copper sheet width and spacing of TD‐GM‐TENG. h) Effect of copper electrode width on transferred charge. i) Effect of the distance between copper electrode and film on transferred charge.
Fundamental physics properties and output performance of TD‐GM‐TENG. a) Comparative schematic diagram of GM‐TENG and TD‐GM‐TENG. b) Charge transfer process of TD‐GM‐TENG with topological defect realized by copper electrode. c) Potential simulation diagram of TD‐GM‐TENG. d) Equivalent circuit diagram of topological defect structure from TD‐GM‐TENG. e) Comparative transferred charge of TD‐GM‐TENG with and without topological defect. f) Comparative number of transferred charge with and without topological defect. g) Comparative waveforms of short‐circuit current with and without topological defect. h) Comparative waveforms of open‐circuit voltage with and without topological defect.
Electrical output performance of TD‐GM‐TENG with different gyro‐multigrid parameters. a) Comparison schematic diagram of the precession and gravitation acceleration effects of TD‐GM‐TENG. b) The relationship between the rotational speed and precession torque. c) The relationship between precession effect and rotation speed. d) The relationship between TD‐GM‐TENG motion angle and transferred charge. e) The relationship between the precession torques at both ends of the shaft. f) Effect of counterweight and diameter of TD‐GM‐TENG on rotation speed. g) Short‐circuit current variation relationship at different acceleration stages. h) Effect of counterweight and motion frequency of TD‐GM‐TENG on horizontal rotation speed. i) Output performance of TD‐GM‐TENG at different horizontal angles. j) Short‐circuit current of TD‐GM‐TENG at different horizontal angles.
Electrical output performance of TD‐GM‐TENG with different structural parameters. a) The output performance of TD‐GM‐TENG with different fur lengths. b) The output performance of TD‐GM‐TENG with different numbers of fur. c) Schematic diagram for stress analysis of fur inclined at 45°. d) Schematic diagram for stress analysis of fur inclined at 90°. e) Schematic diagram for stress analysis of fur inclined at 135°. f) The relationship between furs tilt angle and shaft torque. g) The relationship between rotation speed and transferred charge at different fur tilt angles (45°, 90°, and 135°). h) The relationship between rotation speed and short‐circuit current at different fur tilt angles (45°, 90°, and 135°). i) The relationship between the rotation speed and the counterweight at different fur tilt angles. j) The relationship between different spring lengths and transferred charge.
Application demonstration and comprehensive performance of TD‐GM‐TENG. a) The application scenarios of TD‐GM‐TENG. b) Electrical output performance of TD‐GM‐TENG under different load resistances. c) Comparison of charge density between this work and other works in recent years. d) Output average power and peak power of TD‐GM‐TENG. e) Transferred charge of TD‐GM‐TENG with different structural parameters. f) Relationship between water flow angle and short‐circuit current of TD‐GM‐TENG at different water flow frequencies. g) Comparison of charging voltage of TD‐GM‐TENG in simulated environment and laboratory environment. h) Output stability and durability performance of TD‐GM‐TENG after 10 000 cycles. i) Circuit diagram of ocean emergency power supply system based on TD‐GM‐TENG. j) Application demonstrations of TD‐GM‐TENG supplies power to the alarm and thermometer with 470 µF capacitor.
Gyro‐Multigrid Triboelectric Nanogenerator via Topological Defects Strategy for Efficiently Harvesting Low‐Grade Wave Energy

Wave energy is a promising sustainable energy yet to be fully exploited due to the low frequency and broad‐banded wave fields, so much so that difficult to capture, resulting in low efficiency and limited power output from current many wave energy harvesters. Here, a topological defect gyro‐multigrid triboelectric nanogenerator (TD‐GM‐TENG) is proposed that harnesses the mechanical energy of ocean waves to generate electricity and promotes the accumulation of triboelectric charge on the basis of realized from low to high rotation speed under the precession and gravitation acceleration effects. It benefited from topological defect strategy, TD‐GM‐TENG offers a charge transfer rate of 3.1 µC s⁻¹ that when can reach to a speed of nearly 1000 rpm at the wave frequency of 1 Hz. Furthermore, the charge density reaches 90 µC m⁻² in a cycle of 0.06 s, which is 1.6 times higher than the same kind of spherical‐TENGs in the field of ocean energy harvesting. Finally, TD‐GM‐TENG unit outputs a peak power of 3.7 mW at the simulated water wave environment of 1 Hz and demonstrates its applicability and feasibility of being used as a distributed emergency power supply in the offshoring observation and early warning services.


Plastic Deformation of LiNi0.5Mn1.5O4 Single Crystals Caused by Domain Orientation Dynamics

January 2025

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The nanoscale mechanisms of ion deintercalation in battery cathode materials remain poorly understood, especially the relationship between crystallographic defects (dislocations, small angle grain boundaries, vacancies, etc), device performance, and durability. In this work, operando scanning X‐ray diffraction microscopy (SXDM) and multi‐crystal X‐ray diffraction (MCXD) are used to investigate microstrain and lattice tilt inhomogeneities inside Li1 − x Ni0.5Mn1.5O4 cathode particles during electrochemical cycling and their influence on the material degradation. Using these techniques, microscale lattice degradation mechanisms are investigated inside single crystals, extend it to an inter‐particle scale, and correlate it with the long‐term degradation of the cathode. During cycling, a crystal lattice deformation is observed, associated with phase transitions and inherent lattice defects in the measured particle. Residual misorientations are observed in the structure even after full discharge, indicating an irreversible structural change of the lattice. However, after long‐term cycling such lattice misorientations together with active material dissolution are further exacerbated only in a subset of particles, suggesting high heterogeneity of degradation mechanisms between the cathode particles. Selective degradation of particles could be caused by varying crystal quality across the sample, highlighting the need for a deep understanding of defect microstructures to enable a more rational design of materials with enhanced durability.


a) RT‐XRD patterns of BCFZYN10 and r‐BCFZYN10. XRD Rietveld refinement profiles of b) BCFZYN10 and c) r‐BCFZYN10. d) EDX mapping and e) HR‐TEM images of r‐BCFZYN10.
a) TG, b) O2‐TPD, and c) H2O‐TPD curves of BCFZYN10 and r‐BCFZYN10. d) Dchem and kchem values of BCFZYN10 and r‐BCFZYN10. e) Electrical conductivities of BCFZYN10 and r‐BCFZYN10 from 300 to 800 °C. f) Thermal‐expansion curves of BCFZYN10 and r‐BCFZYN10 at 100–700 °C.
a) Arrhenius plots of ASRs of BCFZYN10 and r‐BCFZYN10 electrodes in 5 vol.% H2O‐air. b) EIS profiles and c) Distribution of relaxation time (DRT) plots of the r‐BCFZYN10 electrode at 500 °C in under various conditions with different steam concentrations. d) DRT profiles of BCFZYN10 and r‐BCFZYN10 electrodes in 5 vol.% H2O‐air at 500 °C. e) ASRs comparison of r‐BCFZYN10 and reported high‐performance air electrodes at below 600 °C. f) The ASR durability test of r‐BCFZYN10 electrode‐based symmetrical cell.
a) I–V and I–P curves of PCFCs with r‐BCFZYN10 electrode at 350–550 °C. b) I–V curves of the r‐PCCs with r‐BCFZYN10 electrode at 450–550 °C in PCFC and PCEC modes (5 vol.% H2O‐air in the air electrode side) c) The comparison of PPDs and electrolysis current densities at 1.3 V for r‐BCFZYN10 and reported high‐performance air electrodes at below 600 °C. Stability tests of r‐PCCs with r‐BCFZYN10 air electrode in d) PCFC and e) PCEC modes at 550 °C.
A New Nanocomposite Electrode Developed from Environmental Atmosphere Triggered Reconstruction for Efficient Reversible Protonic Ceramic Cells

Reversible protonic ceramic cells (r‐PCCs) are highly attractive energy storage and conversion technology, while the insufficient activity of state‐of‐the‐art air electrodes at reduced temperatures strongly limits their practical applications. Herein, this work reports a reduction/re‐oxidation strategy to design a new highly efficient, and durable nanocomposite air electrode for boosting the performance of r‐PCCs operated at intermediate temperatures. Specifically, single‐phase Ba(Co0.4Fe0.4Zr0.1Y0.1)0.9Ni0.1O3‐δ perovskite is selected as the precursor, its treatment in hydrogen atmosphere at 450 °C and then re‐oxidation in air leads to the formation of a nanocomposite, consisted of a perovskite‐based main phase and BaCoO3‐δ and NiO secondary‐phase nanoparticles, where the BaCoO3‐δ phase facilitates oxygen surface exchange while NiO nanoparticles promote surface oxygen/steam adsorption. The corresponding r‐PCC exhibits superior performance at 550 °C in a symmetrical cell (0.162 Ω cm²), a single fuel cell (0.690 W cm⁻²) and an electrolysis cell (−1.066 A cm⁻² at 1.3 V). Such nanocomposite is thermodynamically stable at intermediate temperatures and offers better thermomechanical compatibility with protonic electrolyte because of the reduced thermal expansion coefficient. As a result, superior durability in both fuel and electrolysis cell modes is demonstrated. This study paves a new way for designing outstanding air electrodes for r‐PCCs with great application potential.


Journal metrics


24.4 (2023)

Journal Impact Factor™


22%

Acceptance rate


41.9 (2023)

CiteScore™


11 days

Submission to first decision


$5,510 / £3,670 / €4,600

Article processing charge

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