Wei Zhang’s research while affiliated with Hunan University and other places

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Publications (9)


Different paths for high‐purity CO electrosynthesis from dilute CO2. Path I: CO2 adsorption‐regeneration‐electrolysis‐post‐seperation. Path II: CO2 chemical adsorption‐electrolysis‐post‐seperation. Path III: Electrolysis‐post‐separation. And the porous water‐based path proposed in this work. O: orange, H: green, C: grey, N: blue.
(a) MD simulations of CO2 adsorption in PE. The two‐dimensional snapshot of the simulation box represents the stages after running for 0 ns and 50 ns. Si: brown, O: red (in zeolite) and yellow (in CO2), C: green, and the bulk water phase is shown in a semi‐transparent blue volume. (b) The total CO2 molecule number in the entire system, and the CO2 molecule number in H2O and zeolite‐NC phase. (c) CO2 and H2O molecule number in bulk liquid, bulk gas, and zeolite‐NC region. (d) The interaction energy between zeolite‐NC and CO2 (zeolite‐CO2), zeolite‐NC and H2O (zeolite‐H2O), H2O and CO2 (H2O‐CO2). Error bars correspond to the Standard Deviation of three independent statistics. (e) CO2 adsorption isotherm of PE and corresponding non‐linear fitting. (f) Segmental fitting results for CO2 adsorption isotherm of PE based on intra‐particle diffusion model. Qt is the amount of adsorbed CO2 at a specific time. (g) Schematic illustration for CO2 diffusion in liquid‐film (I) and intra‐particle (II). (h) Schematic of the different regions within zeolite‐NC, and (i) their corresponding CO2 molecule number.
(a) The J and FE at −0.7 V under N2 bubbling before and after adding zeolite‐NC with adsorbed CO2 to 0.1 M KCl solution. (b) The J and CO concentration in the gas product after electrolysis at −0.7 V for 48 hours in PE with physical adsorbed CO2. In situ single‐beam ATR‐FTIR at −0.2 mA for (c) 0.1 M KCl, and (d) PE with physical adsorbed CO2. (e) Schematic illustration for the interfacial CO2 concentration gradient driven CO2 diffusion. OHP is the outer Helmholtz plane. CS, Cδ, and C’ represent the CO2 concentration in the electrode surface, diffusion layer, and bulk phase of the electrolyte. (f) The normalized peak area (SCO2‐X/SCO2‐OCP) at different times. (g) The variations of interfacial CO2 concentrations from A to D points in Figure 3f, for both KCl and PE systems. (h) The CO2 diffusion coefficient for KCl and PE systems.
(a) FE of H2 and CO, (b) JCO for 0.1 M KCl and PE over the Ni−N/C without CO2 bubbling. Error bars correspond to the Standard Deviation of three independent measurements. (c) Cycle performance of CO2 adsorption and electrochemical reduction in PE. (d) DRT analysis of PE at different applied potentials. (e) Comparison of the DRT curves between 0.1 M KCl and PE at −0.6 V. (f) Evolution of the real part capacitance vs. frequency for 0.1 M KCl and PE. (g) The typical infrared spectra of zeolite after immersing in KCl aqueous solution (red line). The contour image is the corresponding variation in peak intensity with the KCl concentrations. (h) Schematic illustration for the local interfacial structure of electrode/PE interface. E represents electrode. (i) In situ ATR‐SEIRAS for monitoring the CO2RR in 0.1 M KCl and PE with physically adsorbed CO2.
(a) Schematic illustration of the circular system for continuous production of high‐purity CO. (b) FECO and (c) JCO in the circular system with 0.1 M KCl and PE under pure/dilute CO2 (15 % CO2). Error bars correspond to the Standard Deviation of three independent measurements. (d) CO purity in the gaseous products of PE‐based circular system under pure and dilute CO2, collected at −0.8 V. (e) Comparison in CO purity for PE and other CO2RR systems. (f) CO purity of Ni−N/C−Ag@Ni foam in PE at different current densities. Error bars correspond to the Standard Deviation of three independent measurements. (g) The long‐term stability of Ni−N/C‐foam electrode (0.25 cm²) in PE‐based circular system at 100 mA cm⁻². (h) Energy consumptions, (i) costs for path I, II, III, and PE path.
Electrolyte Design Using “Porous Water” for High‐purity Carbon Monoxide Electrosynthesis from Dilute Carbon Dioxide
  • Article
  • Publisher preview available

February 2025

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12 Reads

Wei Zhang

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Minyang Dai

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Zhouliangzi Zeng

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Electrosynthesis of high‐purity carbon monoxide (CO) from captured carbon dioxide (CO2) remains energy‐intensive due to the unavoidable CO2 regeneration and post‐purification stages. Here, we propose a direct high‐purity CO electrosynthesis strategy employing an innovative electrolyte, termed porous electrolyte (PE), based on “porous water”. Zeolite nanocrystals within PE provide permanent pores in the liquid phase, enabling physical CO2 adsorption through an intraparticle diffusion model, as demonstrated by molecular dynamics simulations and in situ spectral analysis. Captured CO2 spontaneously desorbs under applied reductive potential, driven by the interfacial CO2 concentration gradient, and is subsequently reduced electrochemically. The high CO2 concentration in PE enhances mass transfer, and surface ion exchange between Si−OH groups and K⁺ ions on the zeolite surface generates a stronger interfacial electric field, promoting electron transfer steps. This optimized kinetics for mass and electron transfer confers heightened intrinsic activity toward CO2 electroreduction. The PE‐based electrolysis system demonstrated superior CO Faradaic efficiency and partial current density compared to the conventional CO2‐fed system. A circular system using PE and a Ni−N/C cathode realized continuous production of high‐purity CO (97.0 wt %) from dilute CO2 (15 %) and maintained >90.0 wt % under 150 mA cm⁻², with significantly reduced energy consumption and costs.

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Electrolyte Design Using "Porous Water” for High‐purity Carbon Monoxide Electrosynthesis from Dilute Carbon Dioxide

February 2025

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6 Reads

Angewandte Chemie

Electrosynthesis of high‐purity carbon monoxide (CO) from captured carbon dioxide (CO₂) remains energy‐intensive due to the unavoidable CO₂ regeneration and post‐purification stages. Here, we propose a direct high‐purity CO electrosynthesis strategy employing an innovative electrolyte, termed porous electrolyte (PE), based on "porous water". Zeolite nanocrystals within PE provide permanent pores in the liquid phase, enabling physical CO₂ adsorption through an intraparticle diffusion model, as demonstrated by molecular dynamics simulations and in‐situ spectral analysis. Captured CO₂ spontaneously desorbs under applied reductive potential, driven by the interfacial CO₂ concentration gradient, and is subsequently reduced electrochemically. The high CO₂ concentration in PE enhances mass transfer, and surface ion exchange between Si–OH groups and K⁺ ions on the zeolite surface generates a stronger interfacial electric field, promoting electron transfer steps. This optimized kinetics for mass and electron transfer confers heightened intrinsic activity toward CO₂ electroreduction. The PE‐based electrolysis system demonstrated superior CO Faradaic efficiency and partial current density compared to the conventional CO₂‐fed system. A circular system using PE and a Ni‐N/C cathode realized continuous production of high‐purity CO (97.0 wt%) from dilute CO2 (15%) and maintained > 90.0 wt% under 150 mA cm‐2, with significantly reduced energy consumption and costs.



High-purity ethylene production via indirect carbon dioxide electrochemical reduction

July 2024

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34 Reads

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11 Citations

High-purity ethylene production from CO2 electroreduction (CO2RR) is a coveted, yet arduous feat because the product stream comprises a blend of unreacted CO2, H2, and other off-target CO2 reduction products. Here we present an indirect reduction strategy for CO2-to-ethylene conversion, one that employs 2-bromoethanol (Br-EO) as a mediator. Br-EO is initially generated from CO2RR and subsequently undergoes reduction to ethylene without the need for energy-intensive separation steps. The optimized AC-Ag/C catalyst with Cl incorporation reduces the energy barrier of the debromination step during Br-EO reduction, and accelerates the mass-transfer process, delivering a 4-fold decrease of the relaxation time constant. Resultantly, AC-Ag/C achieved a FEethylene of over 95.0 ± 0.36% at a low potential of −0.08 V versus reversible hydrogen electrode (RHE) in an H-type cell with 0.5 M KCl electrolyte, alongside a near 100% selectivity within the range of −0.38 to −0.58 V versus RHE. Through this indirect strategy, the average ethylene purity within 6-hour electrolysis was 98.00 ± 1.45 wt%, at −0.48 V (vs RHE) from the neutralized electrolyte after CO2 reduction over the Cu/Cu2O catalyst in a flow-cell.


a) Mechanism of electrochemical conversion of CO2 to CO. b) Models of intrinsic defects with different topological structures. Carbon, hydrogen, and oxygen atoms are tagged as brown, white, and red spheres. The labeled carbon atoms, highlighted by a circle, are adsorbed sites. c) Gibbs free energy diagrams (in eV) of ECR over different defect sites, with the prefix “B” and “E” in the legends indicating the basal and edge region of the carbon plane, respectively. d) CO adsorption energy with bridge and atop adsorption configurations.
a) Schematic illustration of the synthetic routes and the corresponding models of F1100, M1100, F900, and R1100. b) SEM, c) High‐resolution TEM images of F1100. d) A V‐type angle in the highlighted area of the TEM image. e) Raman spectra of F1100, M1100, F900, and R1100. f) C K‐edge XANES, g) EPR spectra of F1100, M1100, F900, and R1100.
CO2 electrochemical reduction test of F1100, M1100, F900, and R1100. a) FECO in a CO2‐saturated 0.1 m KHCO3 aqueous solution. b) FECO and total current density of F1100 in 1 m KOH with flow cell testing. c) The Faradaic efficiency and total current density of F1100 in ionic liquid electrolyte. d) ECSA‐normalized CO partial current densities over the defective carbon electrodes. e) Nyquist plots, and f) Tafel plots of F1100, R1100, M1100, and F900.
a) CO TPD curves of M1100, F900, R1100, and F1100. b) In situ ATR‐SEIRAS spectra of ECR over F1100. c) Schematic illustration of *CO bridge‐adsorbed on double sites over adjacent pentagonal defective sites. d) In situ ATR‐IR spectra of R1100.
Angulated Edge Intrinsic Defect in Carbon as Bridge‐Adsorption Site of CO for Highly Efficient CO2 Electroreduction

February 2024

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22 Reads

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4 Citations

Pervasive intrinsic defects have a significant impact on the electrocatalytic activity of carbon materials, but previous research has focused on the effects of topological structures exclusively. Herein, a compelling demonstration of the pivotal role played by the positions and spatial arrangement of intrinsic defects in determining their efficacy for electrochemical CO2 reduction (ECR) is presented. Theoretical calculations reveal a substantial reduction in energy barriers for *COOH formation at intrinsic defects positioned along the edges while hindering the transformation of *COOH to *CO in the ECR process. To address this issue, a sea urchin‐like nanocarbon (F1100) is designed, which provides adjacent intrinsic defects located in V‐type arranged carbon nanorods. The angulated edge intrinsic defects facilitate the bridge adsorption of carbon monoxide (CO), as confirmed by in situ attenuated total reflection surface‐enhanced infrared absorption spectroscopy, thereby enhancing the specific activity of ECR on intrinsic carbon defects. In a 0.1 m potassium bicarbonate (KHCO3) solution, F1100 achieves a FECO of 95.0%, while in an ionic liquids‐based electrolyte, a current density of 90.0 mA cm⁻² is obtained with nearly complete conversion of CO2 to CO in an H‐type cell.


93% Single-atom Utilization in Base-Resistant Metal-Organic Framework Quantum Dot for Ampere-level CO2 Electroreduction

January 2024

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4 Reads

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4 Citations

Energy & Environmental Science

Single-atom, confined in crystalline porous materials such as metal-organic framework (MOF), features unparalleled multidimensional interactions with the molecular wall of the nano-cavity, showcasing a synergistic catalytic effect. Nevertheless, the insulating...



Versatile Synthesis of Carbon Materials using Protic Ionic Liquids and Salts as Precursors

April 2023

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21 Reads

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1 Citation

The Chemical Record

Carbon materials (CMs) hold immense potential for applications across a wide range of fields. However, current precursors often confront limitations such as low heteroatom content, poor solubility, or complicated preparation and post-treatment procedures. Our research has unveiled that protic ionic liquids and salts (PILs/PSs), generated from the neutralization of organic bases with protonic acids, can function as economical and versatile small-molecule carbon precursors. The resultant CMs display attractive features, including elevated carbon yield, heightened nitrogen content, improved graphitic structure, robust thermal stability against oxidation, and superior conductivity, even surpassing that of graphite. These properties can be elaborate modulated by varying the molecular structure of PILs/PSs. In this Personal Account, we summarize recent developments in PILs/PSs-derived CMs, with a particular focus on the correlations between precursor structure and the physicochemical properties of CMs. We aim to impart insights into the foreseeable controlled synthesis of advanced CMs.


Citations (2)


... Catholyte and anolyte are continuously circulated through the peristaltic pump. Moreover, CO 2 gas directly feeds into the cathode, significantly improving mass transport and boosting production rates [141][142][143][144] . As a result, the thermodynamics and kinetics of CO 2 RR in flow cells differ significantly from those in traditional H-type cells, making flow cells more favorable for large-scale commercial applications [145][146][147] . ...

Reference:

Development of catalysts and reactor designs for CO 2 electroreduction towards C 2+ products
High-purity ethylene production via indirect carbon dioxide electrochemical reduction

... A precise identification of the local structures of nonmetallic species beyond the first coordination shell (n ≥ 2) of metal centers in a heteroatom doping SAC system is still challenging by current characterizing techniques. 49 (Figure 4a). Their most stable configuration and corresponding relative formation energy were explored (Figure 4a and Figure S16). ...

Regulating Nonmetallic Species Beyond the First Coordination Shell of Single-Atom Catalysts for High-Performance Electrocatalysis
  • Citing Article
  • January 2023

Energy & Environmental Science