Rui Yanga,
Yuanhao Lib,
Haonan Xuc,
Qicheng Zhangd,
Shufan Hea,
Tao Shen
a,
Xiaobin Fan
d,
Tao Wu*c and
Yifan Sun
*a
aFrontiers Science Center for Transformative Molecules, School of Chemistry and Chemical Engineering, State Key Laboratory of Synergistic Chem-Bio Synthesis, Zhangjiang Institute for Advanced Study, Shanghai Jiao Tong University, Shanghai 200240, China. E-mail: sunyf@sjtu.edu.cn
bDepartment of Chemistry, University of Pittsburgh, Pittsburgh, PA 15213, USA
cSchool of Chemical Engineering, Dalian University of Technology, Dalian, Liaoning 116024, China. E-mail: taowu@dlut.edu.cn
dSchool of Chemical Engineering and Technology, State Key Laboratory of Chemical Engineering, International Joint Laboratory of Low-carbon Chemical Engineering of Ministry of Education, Tianjin University, Tianjin, 300072, China
First published on 25th August 2025
Adipic acid is an essential platform molecule for polymer production and is industrially manufactured by thermochemical oxidation of the cyclohexanone/cyclohexanol mixture (KA oil). Alternatively, electrifying provides a green and sustainable route to synthesizing adipic acid, but has been restricted by the low catalytic efficiency. Herein, we report that a nickel hydroxide electrocatalyst functionalized with 4,4′-bipyridine (Bipy-Ni(OH)2) delivers a 3-fold greater productivity compared with that of pristine Ni(OH)2, achieving an excellent yield (90%) towards efficient adipic acid electrosynthesis. The experimental and molecular dynamics (MD) simulation results show that Bipy serves as a reservoir to accumulate cyclohexanone, which has low solubility in aqueous solutions. Molecular probe analysis coupled with density functional theory (DFT) calculations demonstrates that Bipy functionalization promotes formation of the key intermediate (2-hydroxycyclohexanone) via modulating the surface electronic characteristics. A Bipy-Ni(OH)2//Ru electro-reforming system in a two-electrode configuration was further constructed to enable concurrent hydrogen and adipate production, revealing its potential for practical applications. Our report demonstrates the efficacy of grafting judicious ligands to electrocatalysts to harness mass transfer and optimize active sites, and the insights can be useful for electrooxidation of a wider scope of organic molecules.
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Scheme 1 Illustration of the (a) thermochemical and (b) proposed electrochemical routes of KA oil oxidation to produce adipic acid. |
Electrocatalytic oxidation provides a competitive route for transforming KA oil into adipic acid under mild conditions using water as the oxygen source and renewable electricity as input energy, meanwhile being coupled with energy-saving H2 generation at cathodes (Scheme 1b). The earliest study of electro-reforming adipate can be traced back to the work of Lyalin and Petrosyan in 2004, in which an adipate yield of 52% was obtained over Ni electrodes by cyclohexanone oxidation.6 Yi et al. later demonstrated that the active sites are NiOOH.7 Since then, great endeavors have been made to develop efficient Ni-based electrocatalysts to improve the yield and (or) selectivity of adipic acid. Strategies such as metal doping (Cu, V, Fe, and Mn)8–11 and defect regulation12 have been reported to improve the yield and/or selectivity of adipate with Ni-based catalysts. For example, OV–NiOOH is reported to facilitate the conversion of cyclohexanone (10 mM) to adipic acid benefiting from facile formation of *OOH on OV sites.12 In another study, Duan and colleagues intercalated sodium dodecyl sulfonate (SDS) into bulk Ni(OH)2 and constructed a hydrophobic microenvironment to accumulate cyclohexanone, obtaining 84% yield of adipic acid with a 20 mM concentration.13 Despite these advances, electrosynthesis of adipic acid suffers from the limited cyclohexanone concentration (typically ≤20 mM), which is far from the industrial high-concentration operation requirements and severely compromises the efficiency and cost benefits for large-scale production.14,15 Achieving high adipic acid yield with a high cyclohexanone concentration is still challenging due to the inherent low solubility of cyclohexanone in aqueous solutions. This poses obstacles to the associated mass transfer and adsorption of cyclohexanone on the catalyst surface, resulting in degraded catalytic performances. Besides, the intricate reaction mechanisms of cyclohexanone oxidation, which include different intermediates with multiple electron and proton transfer steps, also obstruct optimization of the active sites to accelerate the conversion kinetics. Therefore, it is imperative to identify the critical step for elevating the catalytic activity and design efficient Ni-based electrocatalysts towards electrosynthesis of adipic acid at elevated cyclohexanone concentrations.
Molecular functionalization poses a potentially intriguing approach for accessing efficient electrocatalysts for producing adipic acid. Compared with metal doping and defect regulation mediated by the rigid oxide lattice, a wider scope of molecular ligands with tailorable electronic and geometric traits can be explored.16,17 Molecules with heteroatoms like nitrogen, oxygen and sulfur can readily bind with active sites and fine-tune the reaction pathway that leads to higher catalytic activity and selectivity.18–20 However, the influence of molecular functionalization on the structural and electronic properties of Ni(OH)2 and the reaction kinetics of cyclohexanone oxidation remains elusive.
Herein, we report 4,4′-bipyridine-functionalized Ni(OH)2 (Bipy-Ni(OH)2) electrocatalysts for efficient conversion of cyclohexanone (100 mM) to adipic acid. Bipy-Ni(OH)2 results in an excellent yield (90%) and selectivity (91%) towards adipic acid production, achieving a three-fold increase in productivity relative to that of bare Ni(OH)2. The Bipy molecules grafted on Ni(OH)2 enable enrichment of cyclohexanone in NaOH aqueous solutions for subsequent conversions. Mechanistic studies reveal that the cyclohexanone conversion follows hydroxylation at the β site and the subsequent selective Cα–Cβ cleavage pathway, where Bipy functions as an electronic modifier to promote formation of the key intermediate, 2-hydroxycyclohexanone. In a two-electrode system, the Bipy-Ni(OH)2 catalyst delivers 84% yield and 89% selectivity for adipate by KA oil conversion at the anode, along with clean H2 production at the cathode, proving its prominent potential for practical applications.
Fig. 2 summarizes the catalytic performance of Bipy-Ni(OH)2 and Ni(OH)2 towards adipate electrosynthesis from cyclohexanone (100 mM). As depicted in Fig. 2b, Bipy-Ni(OH)2 exhibits an adipate productivity of 270 μmol cm−2 h−1 with 95% faradaic efficiency (FE) at 1.53 V vs. RHE. By sharp contrast, bare Ni(OH)2 delivers one third of adipate productivity (90 μmol cm−2 h−1) with 73% FE, and no activity was observed for the bare Bipy molecule (Fig. S3), collectively highlighting the promotional effect of Bipy functionalization in adipate electrosynthesis. Besides, Bipy-Ni(OH)2 exhibits progressively increased productivities of adipate with increased potentials from 1.43 V to 1.73 V, accompanied by a decrease in FE, which is mainly due to the simultaneous promotion of the competing oxygen evolution reaction (OER). For Ni(OH)2, FE decreases when increasing the potential from 1.43 V to 1.73 V, while the adipate productivity increases and reaches a plateau above 1.63 V. We speculate that this difference can be caused by the low capability of pristine Ni(OH)2 to accumulate cyclohexanone, resulting in a restrictive mass transfer process. In consequence, the added input electricity only promotes the competing OER process. The chronoamperometry results in Fig. 2c show that the current density of Ni(OH)2 experiences a rapid decrease within ∼200 s, which may be due to the fast consumption of cyclohexanone over the Ni(OH)2 surface. In comparison, Bipy-Ni(OH)2 exhibits a much larger current density, implying its better catalysis performance for cyclohexanone oxidation.
In addition to productivity, the yield of adipate under high conversion of cyclohexanone was also evaluated. As shown in Fig. 2d, the content of Bipy has a notable impact on the yield of adipate. A higher or lower Bipy content results in a lower yield, revealing a trade-off between effective molecular functionalization and excessive functionalization blocking the active sites.24,25 The optimized sample exhibits a 90% adipate yield after 10 h electrolysis, highly exceeding that of Ni(OH)2 (49%). The minor by-products include succinic acid and glutaric acid, as determined by the nuclear magnetic resonance (NMR) data for Bipy-Ni(OH)2 (Fig. 2a and e). The selectivity of adipate over Bipy-Ni(OH)2 is calculated to be 91%. Compared with previous reports on adipic acid electrosynthesis, Bipy-Ni(OH)2 offers superior catalytic performance regarding yield, selectivity, and the concentration of cyclohexanone (Fig. 2f and Table S1). The electrochemical active surface areas (ECSAs) of Ni(OH)2 and Bipy-Ni(OH)2 were measured to identify if the enhanced electrocatalytic performance originates from the increase of the surface area due to the ligand-directed nanostructuring or the inherent promotional effect of Bipy functionalization (Fig. S4). Although Bipy-Ni(OH)2 features larger ECSA compared with that of Ni(OH)2, the ECSA-normalized adipate productivity of Bipy-Ni(OH)2 is still higher than that of Ni(OH)2 over potentials ranging from 1.43 V to 1.73 V, highlighting enhancement in the intrinsic catalytic performance of Ni(OH)2 via Bipy functionalization (Fig. 2g).26,27 In addition to Ni(OH)2, Bipy also exhibits evident promotional effects for other Ni-based LDHs regarding adipate yield and FE (Fig. S5).
To elucidate the enrichment behavior of cyclohexanone molecules over different catalyst surfaces, time-dependent molecular dynamics (MD) simulations were conducted.28 As shown in Fig. S6, cyclohexanone molecules exhibit low affinity for the Ni(OH)2 surface, leading to their dispersion (random or aggregated) within the bulk electrolyte. In contrast, nearly all cyclohexanone molecules move towards and accumulate near the Bipy-Ni(OH)2 surface (Fig. 3a). This result indicates that the modified catalyst facilitates the enrichment of cyclohexanone molecules. This enrichment function of Bipy can be further extended to the electrooxidation of a wider array of substrate molecules with limited aqueous solubilities. As displayed in Fig. 3b, for the electrooxidation of C4–C8 cyclic ketone molecules, Bipy-Ni(OH)2 exhibits an observable promotional effect for both productivity and FE of the corresponding products (Table S2). Additional N,N-containing conjugate ligands including 5-nitro-1,10-phenanthroline (Phen-NO2), phthalazine (Ph), 2,2′-bipyridine (2,2′-Bipy) and 1,2-bis(4-pyridyl)ethane (Bpa) were used to functionalize Ni(OH)2 (Fig. 3c), denoted as Phen–NO2–Ni(OH)2, Ph-Ni(OH)2, 2,2′-Bipy-Ni(OH)2, and Bpa-Ni(OH)2, respectively. The successful syntheses of these samples were confirmed by Raman spectroscopy (Fig. S7). All these samples exhibit evident promotional effects both for adipate productivity and FE compared with those of pristine Ni(OH)2 (Fig. 3d), demonstrating universality of the molecular functionalization strategy in improving the catalytic performance of Ni(OH)2 (Fig. S8). Besides, under high conversion, the ligand-facilitated effect is also retained. As shown in Fig. S9, after 10 h of electrocatalysis, the yield of adipate obtained from these molecule-functionalized Ni(OH)2 samples is still higher than that from pristine Ni(OH)2.
Now we have demonstrated the reactant accumulation capability of Bipy functionalization and its promotional effect on adipate electrosynthesis. In order to investigate the other roles of Bipy functionalization, the primary task is to pinpoint the reaction path in our system. Industrially, cyclohexanone and cyclohexanol mixtures serve as crude materials to produce adipate. Controlled experiments were performed to understand the difference between cyclohexanone and cyclohexanol upon electrooxidation. The NMR results show that cyclohexanol first undergoes a 2e− oxidation step to generate the cyclohexanone intermediate, which is further oxidized to adipate via C–C cleavage. This pathway is the same for both Ni(OH)2 and Bipy-Ni(OH)2 (Fig. S10a). After 14 h of electrolysis, 88.6% and 46.1% yields of adipate can be obtained over the Bipy-Ni(OH)2 and Ni(OH)2 catalysts (Fig. S10b). To evidence the transformation process of cyclohexanol to cyclohexanone before obtaining adipate, 1-methylcyclohexanol was chosen as the substrate molecule given its incapability of being oxidized to ketone. As a result, there is no obvious change in 1-methylcyclohexanol before and after electrolysis (Fig. S11). This directs us to focus on the conversion process from cyclohexanone to adipate.
The above results together with previous reports point out three possible reaction pathways for cyclohexanol oxidation (Fig. 4a). The first path involves 1,2-cyclohexanedione as a crucial intermediate for the following oxidative C–C cleavage between the two neighboring carbonyl groups to produce adipate (Path 1).29 The second path indicates that cyclohexanone undergoes hydroxylation at the β site and C–C cleavage before dione formation8,9 (Path 2). In the third one, cyclohexanone is oxidized to form the ε-caprolactone intermediate by the Baeyer–Villiger oxidation and ε-caprolactone undergoes subsequent hydrolysis and oxidation to produce adipate (Path 3).12 We first applied 1,2-cyclohexanedione as the substrate molecule which mainly results in glutarate, thus ruling out Path 1. Furthermore, electrolysis of 1,3-cyclohexanedione and 1,4-cyclohexanedione leads to formation of a mixture of glutarate and succinate, and succinate as the major product (Fig. S12 and S13), respectively, thus excluding dione being the key intermediate. To distinguish between Path 2 and Path 3, we conducted electron paramagnetic resonance (EPR) spectroscopy using 5,5-dimethyl-1-pyrroline N-oxide (DMPO) as the capturer to identify the as-formed radical species during the electro-oxidation process.30 As shown in Fig. 4b, hydroxyl (⋅OH) and carbon-centered radicals (C⋅) were observed in our case. Only ⋅OH was detected in the absence of cyclohexanone (Fig. S14), suggesting that C⋅ originates from cyclohexanone. This implies that cyclohexanone first undergoes β-H elimination to form C⋅ and subsequently yields 2-hydroxycyclohexanone through oxygenation by ⋅OH. Hydroperoxyl radicals (⋅OOH), which are absent in our case, would be expected following Path 3. Therefore, Path 2 involving 2-hydroxycyclohexanone formation is identified as the major pathway in our case (Fig. 4c). To verify whether Bipy functionalization also influences the following oxidation process, we applied 2-hydroxycyclohexanone as the starting electrocatalysis material. For the 4 h electrolysis, the adipate yield for the electrooxidation of 2-hydroxycyclohexanone using Ni(OH)2 and Bipy-Ni(OH)2 is 75% and 87%, respectively, both higher than that using cyclohexanone as the substrate (27% for Ni(OH)2 and 66.6% for Bipy-Ni(OH)2 (Fig. 4d). The notably faster transformation speed indicates that the breaking of Cα–Cβ becomes feasible once Cα and Cβ reach a high oxidation state.8 The promotional effect of Bipy-Ni(OH)2 on the oxidation of 2-hydroxycyclohexanone may be due to the enhanced oxidizing power resulting from electronic modification induced by Bipy functionalization. This is further supported by the oxidation result of 1,6-hexanediol (Fig. S15).
The above results suggest that the conversion from 2-hydroxycyclohexanone to adipate in Path 2 is favorable. We thereby reason that the way towards the 2-hydroxycyclohexanone formation is the key step that leads to distinct catalytic performances of Ni(OH)2 and Bipy-Ni(OH)2. Density functional theory (DFT) calculations were adopted to compare the energetic barrier from cyclohexanone to 2-hydroxycyclohexanone over the pristine and functionalized Ni(OH)2 catalyst. As displayed in Fig. 4e and S16, Ni(OH)2 exhibits a 0.7 eV barrier for pristine Ni(OH)2, while the value decreases to 0.57 eV for Bipy-Ni(OH)2 (barrier refers to the minima of the different products coordinated to the different Ni sites). This implies that the electronic modulation of Bipy on Ni(OH)2 facilitates the formation of 2-hydroxycyclohexanone.31 Based on this experimental and computational evidence, we attribute the crucial role of Bipy functionalization to facilitating production of the key intermediate (2-hydroxycyclohexanone) via electronic regulations.
Besides, to gain insights into the structure transformation and clarify the actual active sites, we employed in situ Raman spectroscopy (Fig. S17). As shown in Fig. 4f, upon applying anodic potentials in 1.5 M NaOH, evolution of the Eg bending and A1g stretching mode of Ni3+–O was observed, along with leaching of the Bipy molecule, evidencing a total restructuring from Ni(OH)2 to NiOOH under OER conditions,32,33 while in 0.1 M cyclohexanone, with the increase of potentials, no obvious Bipy dissolution is observed (Fig. 4g). The difference between the Raman spectra at the open-circuit voltage (OCV) in NaOH (1.5 M) and that in NaOH (1.5 M) + cyclohexanone (100 mM) is due to the overlap of the peak features of cyclohexanone and Bipy.34 Besides, the Ni3+–O signals under cyclohexanone oxidation conditions emerged at higher voltage compared with that of the OER conditions. This implies that the Ni3+–O species serve as redox mediators during the cyclohexanone oxidation process, causing partial consumption of Ni3+–O species.9,35–37
Towards practical applications, we coupled the Bipy-Ni(OH)2 catalyst with a Ru hydrogen evolution catalyst to construct a two-electrode electro-reforming system for concurrent hydrogen and adipate production at the cathode and anode, respectively. In order to simulate industrial scenarios, KA oil composed of cyclohexanol and cyclohexanone (3:
2) was chosen as the starting material. As shown in Fig. 5a, the system with KA oil delivers a more energy-saving process compared with that of the water splitting one with a nearly 155 mV potential decrease at 30 mA cm−2, corresponding to ∼9% energy saving. Favorable kinetics with a smaller Tafel slope (166.1 mV dec−1) was also achieved with the KA oil system relative to that of the water splitting process (199.4 mV dec−1, Fig. S18). For the electrolysis of KA oil at 1.8 V, an 84% yield and 89% selectivity of adipate acid at the anode and pure H2 generated at the cathode can be achieved (Fig. 5b and S19a), demonstrating the practical potential of Bipy-Ni(OH)2. The stability of the Bipy-Ni(OH)2//Ru catalyst was further evaluated with the long-term (40 h) electrolysis measurement (Fig. 5c). For each 4 h cycle, the current density gradually decreases due to consumption of the reactant (KA oil) and instantly recovers upon the electrolyte refresh. The TON was estimated to be 535 per Ni-site (Fig. S19b). A slight decrease in current density over the long term indicated reasonable stability of the electrode material.
Our work emphasizes the significance of molecular functionalization of solid electrocatalysts for enhanced performance. The organic–inorganic interface affords a diverse platform for harnessing the mass transfer behavior of reactants and optimizing the metal active sites. It is anticipated that more molecular ligands can be explored as both catalytically tunable modifiers and effective hydrophobic agents for enhanced catalysis. The molecular functionalization strategy can be further extended to supported heterogeneous catalysts, for which the metal–support interactions may be tailored with molecular precision.
Supplementary information: experimental and calculation details, additional material characterization and electrosynthesis results, and performance comparison. See DOI: https://doi.org/10.1039/d5sc05036g.
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