In the field of CO catalytic oxidation, both copper oxide (CuO) and manganese dioxide (MnO₂) are commonly used non-noble metal catalysts. However, each has shortcomings when used alone: CuO exhibits high activity but is prone to sintering and has poor water resistance; MnO₂ offers better thermal stability but relatively low low-temperature activity. When the two are combined to form a CuO-MnO₂ composite catalyst (the basic system of Hopcalite), the CO oxidation activity is much higher than the sum of the physical mixture of the two individual components. This “1+1>2” phenomenon is called the synergistic effect. Understanding the nature of this synergy is of great significance for optimizing catalyst formulations and reducing reliance on precious metals.
The synergistic effect of copper-manganese composite catalysts mainly derives from the following aspects:
During CO catalytic oxidation, the active sites must undergo a redox cycle. In single CuO, the valence change of copper is mainly Cu²⁺ ↔ Cu⁺, while in single MnO₂, manganese changes as Mn⁴⁺ ↔ Mn³⁺. When the two are combined, an electron pair synergy of Cu⁺ + Mn⁴⁺ ↔ Cu²⁺ + Mn³⁺ is formed. This cycle greatly accelerates the electron transfer rate, allowing the catalyst to transition more quickly from the oxidized state to the reduced state, thereby lowering the activation energy for CO oxidation. X-ray photoelectron spectroscopy (XPS) analysis confirms that the proportions of Cu⁺ and Mn³⁺ in the CuO-MnO₂ composite catalyst are significantly higher than in the single components, indicating strong electronic interaction at the interface.
CO catalytic oxidation follows the Mars–van Krevelen (MvK) mechanism: CO reacts with lattice oxygen on the catalyst surface to produce CO₂, leaving an oxygen vacancy; then gas-phase O₂ fills the vacancy, regenerating the catalyst. The concentration and mobility of oxygen vacancies are key factors determining catalytic activity. When CuO and MnO₂ are combined, lattice distortion occurs due to differences in ionic radii and electronegativity, generating more defect sites and oxygen vacancies. Electron paramagnetic resonance (EPR) studies show that the oxygen vacancy concentration in CuO-MnO₂ composite catalysts is 2-3 times that of pure CuO. These oxygen vacancies not only provide adsorption and activation sites for CO but also accelerate the bulk migration of lattice oxygen.
At the interface between CuO and MnO₂, copper and manganese atoms are arranged adjacently, forming unique bimetallic sites. CO molecules tend to adsorb on Cu⁺ sites, while O₂ is more easily activated near Mn⁴⁺ sites. This spatial division of labor makes the reaction pathway more efficient: after CO adsorbs on a Cu site, the adjacent Mn site provides active oxygen that can rapidly react with it. In situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) observations show that the shift and intensity changes of the CO adsorption peak on the composite catalyst surface indicate significantly stronger synergistic adsorption ability of the bimetallic sites compared to single components.
Single CuO is prone to grain growth and loss of surface area at high temperatures. MnO₂ acts as a structural stabilizer, effectively isolating CuO particles and inhibiting their migration and agglomeration. Thermogravimetric-differential thermal analysis (TG-DTA) shows that the phase transition temperature of the CuO-MnO₂ composite catalyst is about 80–100°C higher than that of pure CuO. This gives the composite catalyst better resistance to sintering when reaction temperatures fluctuate or localized overheating occurs.
Not every mixing ratio produces the strongest synergy. Studies indicate that when the Cu/Mn molar ratio is between 1:2 and 2:1, the composite catalyst exhibits the highest CO oxidation activity.
| Cu:Mn Molar Ratio | CO Conversion (25°C, GHSV 3000h⁻¹) | Surface Area (m²/g) | Main Phases |
|---|---|---|---|
| 0:1 (pure MnO₂) | 52% | 85 | MnO₂ |
| 1:3 | 78% | 110 | MnO₂ + small amount of CuO |
| 1:2 | 94% | 135 | Cu₁.₅Mn₁.₅O₄ spinel phase |
| 1:1 | 98% | 128 | CuMn₂O₄ + CuO |
| 2:1 | 91% | 102 | CuO + CuMn₂O₄ |
| 3:1 | 75% | 88 | CuO + small amount of manganese oxide |
| 1:0 (pure CuO) | 45% | 42 | CuO |
The data show that when Cu:Mn is close to 1:1, the composite catalyst forms the copper‑manganese spinel (CuMn₂O₄) phase, which exhibits the strongest synergy. In the spinel structure, copper ions occupy tetrahedral sites and manganese ions occupy octahedral sites, allowing electrons to transfer quickly through oxygen bridges while generating abundant oxygen vacancies. Therefore, industrial Hopcalite catalysts typically use a Cu:Mn ratio of approximately 1:1 to 1:2.
Even with the same chemical composition, different preparation methods can produce composite catalysts with significantly different synergy.
A mixed solution of copper and manganese salts and an alkali solution (e.g., NaOH or Na₂CO₃) are added simultaneously while controlling pH and temperature to obtain a copper‑manganese hydroxide precursor, which is then calcined to form the composite oxide. The coprecipitation method achieves atomic‑level uniform mixing, favors the formation of the spinel phase, and produces the strongest synergistic effect. Studies show that the CO conversion of CuO-MnO₂ catalysts prepared by coprecipitation is 15‑20% higher than that of impregnation‑prepared catalysts.
MnO₂ support is prepared first, then impregnated with a copper salt solution, dried, and calcined. In this method, copper is mainly distributed on the surface of MnO₂, resulting in limited interfacial contact and weaker synergy than the coprecipitation method.
Commercial CuO and MnO₂ powders are simply mixed and ground. Due to the lack of intimate interfacial contact, electronic synergy is weak, and the activity is far lower than that of coprecipitated samples. This confirms that the synergistic effect arises from atomic/nanoscale interfacial interaction, not from macroscopic mixing.
The calcination temperature determines the degree of spinel phase formation. At 300°C, some amorphous phases remain; at about 450°C, the spinel phase is fully developed and activity is highest; above 600°C, CuMnO₃ or other inert phases form, surface area drops sharply, and the synergy weakens.
Taking room‑temperature CO catalytic oxidation as an example, the long‑term performance of pure CuO, pure MnO₂, and the CuO-MnO₂ composite catalyst (Cu:Mn=1:1, coprecipitation) are compared:
In addition, the performance loss of the composite catalyst in an atmosphere containing a small amount of CO₂ (5%) is much smaller than that of pure CuO, because the presence of manganese inhibits carbonate formation. These advantages make CuO-MnO₂ composite catalysts the preferred material for applications such as mine refuge chambers, respirators, and industrial exhaust gas treatment.
The synergistic effect between copper oxide and manganese dioxide originates from electronic interaction, increased oxygen vacancies, and synergistic adsorption at bimetallic interfacial sites. The optimal Cu:Mn molar ratio is approximately 1:1 to 1:2, and coprecipitation is the preferred preparation method for achieving strong synergy. Understanding and utilizing this synergistic effect allows the development of efficient and stable CO catalysts without relying on precious metals, offering significant economic and environmental value. Future research directions include: doping with a third element (e.g., cerium, cobalt) to further enhance synergy; developing novel nanostructures to expose more interfaces; and verifying the durability of the synergistic effect under complex industrial conditions such as sulfur‑containing and high‑humidity environments.
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