Houjun Chen’s research while affiliated with Hunan University and other places

What is this page?


This page lists works of an author who doesn't have a ResearchGate profile or hasn't added the works to their profile yet. It is automatically generated from public (personal) data to further our legitimate goal of comprehensive and accurate scientific recordkeeping. If you are this author and want this page removed, please let us know.

Publications (6)


(a) XRD patterns, (b) N2 adsorption‐desorption curves of Co3O4 and D‐Co3O4. The high‐resolution XPS (c) Co 2p, and (d) O 1s spectra of Co3O4 and D‐ Co3O4. (e) EPR spectra, and (f) Raman spectra for Co3O4 and D‐Co3O4.
(a–b) HRTEM images of Co3O4. (c–f) The IFFT patterns for the selected red and blue box in (a) and (b), and their corresponding integrated pixel intensity profile. (g) HRTEM image of D‐Co3O4. (h) The intensity profile for the line A direction in (g). (i) False color image of D‐Co3O4.
(a) Infrared images of Co3O4 (up) and D‐Co3O4 (down) under the 808 nm light irradiation. (b) LSV curves for Co3O4 and D‐Co3O4 with and without laser irradiation in 0.1 M KOH containing 50 mM HMF. (c) Comparisons about the potentials and current density for reported typical catalysts and our work. (d) The high‐performance liquid chromatography spectra for electrolyte after electrolysis with different durations over the D‐Co3O4‐3W. (e) The concentration of HMF and the different intermediates/products collected at different times of D‐Co3O4‐3W. (f) The cycle performance of D‐Co3O4‐3W. (g) The variation of current density under alternately switched laser irradiation for Co3O4 and D‐Co3O4. (h) Differences in charging and discharging current density were plotted against scan rates for Co3O4 and D‐Co3O4 with and without laser irradiation. (i) The ECSA normalized current density for Co3O4 and D‐Co3O4 with and without laser irradiation.
(a) Variations of open‐circuit potentials of Co3O4 and D‐Co3O4 when 50 mM HMF was injected and the laser irradiation applied. (b) CV curves for evaluating the OH⁻ adsorption over Co3O4 and D‐Co3O4 with and without light irradiation. Bode plots acquired by in situ electrochemical impedance spectroscopy for (c) Co3O4 and (d) D‐Co3O4. (e) Two oxidation pathways of HMF. In situ ATR‐SEIRAS for HMF oxidation over (f) Co3O4, and (g) D‐ Co3O4.
(a) Schematic illustration of the photothermal assisted HMF oxidation paired CO2 electroreduction system. (b) Cathodic CO selectivity, and (c) anodic FDCA selectivity at different cell potentials. (d) The cell potentials for achieving different current densities.
Photothermal Assisted Biomass Oxidation for Pairing Carbon Dioxide Electroreduction with Low Cell Potential
  • Article
  • Publisher preview available

October 2024

·

17 Reads

Houjun Chen

·

Rongcheng Peng

·

Ting Hu

·

[...]

·

Integrating anodic biomass valorization with carbon dioxide electroreduction (CO2RR) can produce value‐added chemicals on both the cathode and anode; however, anodic oxidation still suffers from high overpotential. Herein, a photothermal‐assisted method was developed to reduce the potential of 5‐hydroxymethyl furfural (HMF) electrooxidation. Capitalizing on the copious oxygen vacancies, defective Co3O4 (D‐Co3O4) exhibited a stronger photothermal effect, delivering a local temperature of 175.47 °C under near infrared light illumination. The photothermal assistance decreased the oxidation potential of HMF from 1.7 V over pristine Co3O4 to 1.37 V over D‐Co3O4 to achieve a target current density of 30 mA cm⁻², with 2,5‐furandicarboxylic acid as the primary product. Mechanistic analysis disclosed that the photothermal effect did not change the HMF oxidation route but greatly enhanced the adsorption capacity of HMF. Meanwhile, faster electron transfer for direct HMF oxidation and the surface conversion to cobalt (oxy)hydroxide, which contributed to indirect HMF oxidation, was observed. Thus, rapid HMF conversion was realized, as evidenced by in situ surface‐enhanced infrared spectroscopy. Upon coupling cathodic CO2RR with an atomically dispersed Ni−N/C catalyst, the Faradaic efficiencies of CO (cathode) and 2,5‐furandicarboxylic acid (FDCA, anode) exceeded 90.0 % under a low cell potential of 1.77 V.

View access options

High-purity ethylene production via indirect carbon dioxide electrochemical reduction

July 2024

·

36 Reads

·

12 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.


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

January 2024

·

5 Reads

·

6 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...


Molecular engineering strategy for cation solvation structure toward highly selective CO2RR.
Characterization for electrolyte microstructure. Snapshots of (a) KCl‐DMSO‐5 and (b) KCl‐CH3CN‐5 electrolyte molecular system obtained from MD simulation. Atom color coding: red: O, white: H, yellow: S, cyan: C, orange: K. (c) Local structure of KCl‐DMSO‐5 (top) and KCl‐CH3CN‐5 (bottom) obtained from MD simulation. RDFs of (d) KCl‐DMSO‐5 and (e) KCl‐CH3CN‐5. (f) In situ ATR‐SEIRAS of the N2‐saturated KCl‐DMSO‐5 system in the range from 1000 to 1380 cm⁻¹, and (g) its corresponding contour image. (h) In situ ATR‐SEIRAS of the N2‐saturated KCl‐CH3CN‐5 system. The potentials ranged from −0.15 to −1.35 V with an interval of −0.1 V. (i) Evolution of the real part capacitance vs. frequency for pristine KCl, KCl‐DMSO‐5, and KCl‐CH3CN‐5 electrolyte at −0.45 V.
Electrochemical performance. (a) LSV curves of N2‐saturated KCl‐DMSO‐x. (b) Online gas chromatography analysis of reduction products for N2‐saturated KCl‐DMSO‐x electrolyte at −0.8 V and the standard sample. The inset is the magnified spectrum within the retention time from 5 to 7 min. (c) H2 selectivity of the CO2‐saturated KCl‐DMSO‐x system at −0.75 V. (d) Heatmaps of CO partial current density at −0.75 V and −0.85 V in KCl‐DMSO‐x electrolyte. FE of H2 and CO in (e) CO2‐saturated 0.5 M KCl and KCl‐DMSO‐5, and (f) CO2‐saturated 0.5 M KCl and KCl‐CH3CN‐5. (g) Variation of FEH2 after adding 5 M DMSO or 5 M CH3CN in 0.5 M KCl at different potentials. (h) The kinetic current density of HER in KCl‐DMSO‐x. (i) Arrhenius plots of CO formation over an Ag electrode in 0.5 M KCl, KCl‐DMSO‐5, and KCl‐CH3CN‐5.
Understanding the changes in interfacial H2O structure. Snapshots of (a) KCl‐DMSO‐5, (b) KCl‐CH3CN‐5 between two Ag electrodes from MD simulation at −1.1 V, and (c) the corresponding density distribution of H2O. Deconvolution of the experimental O−H stretching vibration peaks in ATR‐FTIR for (d) KCl‐CH3CN‐5 and (e) KCl‐DMSO‐5. (f) Fraction of free H2O and H2O in hydration shell for KCl‐DMSO‐5 and KCl‐CH3CN‐5. (g) Cϕ at various overpotentials for 0.5 M KCl, KCl‐CH3CN‐5, and KCl‐DMSO‐5. Inset shows the corresponding QH*.
Exploring the enhanced intrinsic activity for CO2RR. In situ ATR‐SEIRAS for (a) KCl‐DMSO‐5, and (b) KCl‐CH3CN‐5. (c) KIE of H/D for CO2‐to‐CO conversion at different potentials for KCl‐CH3CN‐5 and KCl‐DMSO‐5. (d) Gibbs free energy changes of CO2‐to‐CO conversion over Ag(200) and Ag(220) plane in electrolyte with and without DMSO additive. (e) The models of *CO2+*H2O on Ag(200) and Ag(200)‐DMSO sites. (f) The adsorption energy of the H2O molecule on the Ag site with adsorbed CO2. (g) Energy barriers of transitional state formation for *CO2‐to‐*COOH conversion over Ag electrode in electrolyte with and without DMSO additive. (h) The acquired transitional state models of *CO2+H(TS).
Molecular Engineering of Cation Solvation Structure for Highly Selective Carbon Dioxide Electroreduction

August 2023

·

47 Reads

·

32 Citations

Balancing the activation of H2O is crucial for highly selective CO2 electroreduction (CO2RR), as the protonation steps of CO2RR require fast H2O dissociation kinetics, while suppressing hydrogen evolution (HER) demands slow H2O reduction. We herein proposed one molecular engineering strategy to regulate the H2O activation using aprotic organic small molecules with high Gutmann donor number as a solvation shell regulator. These organic molecules occupy the first solvation shell of K⁺ and accumulate in the electrical double layer, decreasing the H2O density at the interface and the relative content of proton suppliers (free and coordinated H2O), suppressing the HER. The adsorbed H2O was stabilized via the second sphere effect and its dissociation was promoted by weakening the O−H bond, which accelerates the subsequent *CO2 protonation kinetics and reduces the energy barrier. In the model electrolyte containing 5 M dimethyl sulfoxide (DMSO) as an additive (KCl‐DMSO‐5), the highest CO selectivity over Ag foil increased to 99.2 %, with FECO higher than 90.0 % within −0.75 to −1.15 V (vs. RHE). This molecular engineering strategy for cation solvation shell can be extended to other metal electrodes, such as Zn and Sn, and organic molecules like N,N‐dimethylformamide.


Molecular Engineering of Cation Solvation Structure for Highly Selective Carbon Dioxide Electroreduction

July 2023

·

14 Reads

·

8 Citations

Angewandte Chemie

Balancing the activation of H 2 O is crucial for highly selective CO 2 electroreduction (CO 2 RR), as the protonation steps of CO 2 RR require fast H 2 O dissociation kinetics, while suppressing hydrogen evolution (HER) demands slow H 2 O reduction. We herein proposed one molecular engineering strategy to regulate the H 2 O activation using aprotic organic small molecules with high Gutmann donor number as a solvation shell regulator. These organic molecules occupy the first solvation shell of K ⁺ and accumulate in the electrical double layer, decreasing the H 2 O density at the interface and the relative content of proton suppliers (free and coordinated H 2 O), suppressing the HER. The adsorbed H 2 O was stabilized via the second sphere effect and its dissociation was promoted by weakening the O−H bond, which accelerates the subsequent *CO 2 protonation kinetics and reduces the energy barrier. In the model electrolyte containing 5 M dimethyl sulfoxide (DMSO) as an additive (KCl‐DMSO‐5), the highest CO selectivity over Ag foil increased to 99.2 %, with FE CO higher than 90.0 % within −0.75 to −1.15 V (vs. RHE). This molecular engineering strategy for cation solvation shell can be extended to other metal electrodes, such as Zn and Sn, and organic molecules like N,N‐dimethylformamide.


Citations (4)


... 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

... Although these high value chemicals and high energy density fuels have broad markets, industrial-scale implementation of CO 2 RR still has a long way to go 4 . On the one hand, in aqueous media, water (H 2 O) molecules serve as the proton source for electrochemical reactions, leading to a conflict between CO 2 RR and hydrogen evolution reaction (HER) [5][6][7][8] . The proton-electron coupling properties of CO 2 RR require effective activation of H 2 O and smooth proton transfer to avoid excessive activation of H 2 O, otherwise HER would competitively overwhelm CO 2 RR. ...

Molecular Engineering of Cation Solvation Structure for Highly Selective Carbon Dioxide Electroreduction

... Particularly, near-unity conversion of Br-EO to ethylene was obtained from −0.38 to −0.58 V (vs RHE, Fig. S11). Ag has also shown significant efficacy in the CO 2 -to-CO conversion as previously reported 46,47 , but no discernible formation of CO was observed in our present investigation due to the carefully chosen reduction potentials and the marked predilection for reduction of Br-EO (Fig. S12). The ethylene production rate of AC-Ag/C was estimated to be 1.57 ...

Molecular Engineering of Cation Solvation Structure for Highly Selective Carbon Dioxide Electroreduction
  • Citing Article
  • July 2023

Angewandte Chemie