Application of Copper Oxide Catalysts in the Thermal Catalytic Oxidation of Low-Concentration Methane

1. مقدمة

Methane is the second largest greenhouse gas, with a global warming potential approximately 28 times that of carbon dioxide. In coal mining operations, large quantities of low-concentration methane (typically below 1 المجلد٪) are directly vented to the atmosphere as ventilation air methane (VAM), causing significant greenhouse effects and wasting substantial energy resources. Due to the extremely high structural stability of the methane molecule (C–H bond energy ≈ 439 كيلوجول / مول), and the large volume and low heating value of low-concentration methane, direct combustion is not feasible, posing considerable technical challenges for abatement.

Catalytic oxidation technology enables complete methane oxidation at temperatures far below its auto‑ignition point, making it one of the most promising approaches for treating low‑concentration methane. Among various catalyst systems, أكسيد النحاس (النحاس)‑based catalysts have attracted widespread attention due to their low cost, توافر وفيرة, وخصائص الأكسدة والاختزال القابلة للضبط. This article systematically reviews the research and application status of CuO catalysts in the thermal catalytic oxidation of low‑concentration methane, covering catalytic mechanisms, performance characteristics, industrial progress, and future challenges.

محفز أكسيد النحاس

2. Catalytic Oxidation Mechanism

The catalytic oxidation of methane over copper oxide catalysts follows the Mars–van Krevelen (إم في كيه) mechanism. The core feature of this mechanism is that the catalytic reaction proceeds via participation of lattice oxygen from the catalyst, with gas‑phase oxygen replenishing the consumed lattice oxygen to complete a continuous catalytic cycle.

خاصة, the reaction involves the following steps:

Step 1 – Oxygen adsorption and activation: Gas‑phase oxygen molecules adsorb onto the CuO_س catalyst surface and dissociate into reactive oxygen atoms.

Step 2 – C–H bond activation of methane: Methane molecules interact with reactive oxygen species on the catalyst surface, leading to cleavage of the C–H bond. Studies indicate that methane activation on the CuO(111) surface involves a pair of under‑coordinated copper atoms and lattice oxygen atoms, whose synergistic effect significantly lowers the activation barrier compared to a clean copper surface.

Step 3 – Oxidation and desorption: The activated methane molecules are progressively oxidized to intermediates (على سبيل المثال, methoxy Cu–OCH₃, formate Cu–OOCH, إلخ.) and finally fully oxidized to carbon dioxide and water.

Step 4 – Lattice oxygen regeneration: The consumed lattice oxygen is replenished by gas‑phase oxygen molecules, restoring the catalyst to its initial state for the next catalytic cycle.

Within this mechanistic framework, ال تركيز الشغور الأكسجين و lattice oxygen mobility of the catalyst are key factors determining catalytic activity. Higher oxygen vacancy density enhances the catalyst’s ability to adsorb and activate oxygen, thereby accelerating the MvK cycle.

3. Performance of Copper Oxide Catalysts

3.1 Supported CuO_س/zeolite catalysts

Highly dispersed CuO_س species (loading ≈ 6 نسبة الوزن) supported on mordenite (MOR) zeolite exhibit excellent performance in low‑concentration methane oxidation. The optimized catalyst achieves 100% complete oxidation of methane to CO₂ at 400°C, with a T₁₀ (درجة الحرارة ل 10% تحويل) as low as 230°C and a T₉₀ (درجة الحرارة ل 90% تحويل) of 350°C. During 100 hours of continuous reaction, the catalyst maintained outstanding long‑term stability and reusability.

The enhanced performance is mainly attributed to four factors:

• Promotion by acidic sites: Increased Brønsted acid sites on the catalyst facilitate methane adsorption and dissociation;
• Anchor effect of the support: Al³⁺ ions in the support serve as anchoring sites, effectively dispersing CuO_س species and providing more active sites;
• Oxidation state modulation: Changes in preparation conditions (على سبيل المثال, pH) can tune the oxidation state of the catalyst; alkaline conditions favor the formation of more Cu⁺ والنحاس⁰ active species;
• Resistance to coking and sintering: Brønsted acid sites mitigate low‑temperature coking and also prevent loss of structural stability at high temperatures.

3.2 CuO-CeO₂ composite oxide catalysts

CuO-CeO₂ composite oxides prepared by the sol‑gel method were evaluated in catalytic combustion of 1% CH₄, 78% N₂, و 21% يا₂ (simulated atmosphere). The activity order was CuO-CeO₂ > النحاس > CeO₂.

The significant enhancement by CeO₂ addition is mainly due to two reasons:

• Improved dispersion: Ce ions promote the highly dispersed distribution of Cu species on the catalyst surface;
• Oxygen storage capacity: The reversible Ce³⁺/م⁴⁺ redox cycle enhances the catalyst’s oxygen storage and release capability, making lattice oxygen replenishment more efficient and thus accelerating the MvK catalytic cycle.

Further kinetic studies indicate that methane oxidation over the CuO‑CeO₂ catalyst follows the Langmuir‑Hinshelwood mechanism, where adsorbed CH₄ reacts with adsorbed O₂ on the catalyst surface.

3.3 Comparison with other transition metal oxides

In a comparative study of transition metal oxides supported on open‑cell foam carriers, the activity order was: NiO > الحديد₂يا₃ ≈ Co₃يا₄ > من₂يا₃ > النحاس > Cr₂يا₃. Although CuO does not exhibit the highest activity among its transition metal oxide counterparts, its cost advantage و resource availability are significantly superior to metals like Ni and Co. علاوة على ذلك, its catalytic performance can be greatly improved through support selection and composite modification (على سبيل المثال, with CeO₂). This gives CuO‑based catalysts a unique economic edge in large‑scale industrial applications.

4. Industrial Application Progress

4.1 Coal mine ventilation air methane treatment

Coal mine ventilation air is the largest source of low‑concentration methane emissions. For VAM with methane concentrations in the range of 0.1%–1.2%, monolithic catalysts can achieve methane conversion > 95% at 350–600°C, with an overall catalyst lifetime of up to two years.

حالياً, أ pilot‑scale demonstration of 1000 Nm³/ح has been completed, and the process design capacity for 30,000–60,000 Nm³/ح is available, currently in the demonstration development stage. This technical route provides new options for heating mine roadways in winter, district heating, and employee bathing facilities in low‑concentration gas mining areas.

Case study: In a coal mine VAM treatment project, the catalytic oxidation process was applied to treat ventilation air with methane concentration below 0.5%. Operational data showed that under conditions of inlet temperature around 400°C and space velocity approximately 10,000 ح^-1, methane conversion remained stable above 90% for more than 1,000 ساعات من التشغيل المتواصل. The treated tail gas methane concentration dropped below emission limits, while the heat released from the reaction was recovered via a waste heat recovery system for district heating, achieving both environmental and energy benefits.

4.2 Natural gas engine exhaust purification

Natural gas engine exhaust also contains unburned methane. Since exhaust temperatures are typically below 550°C and contain certain amounts of water vapor and sulfur compounds, high demands are placed on low‑temperature activity and poison resistance of the catalyst. CuO‑based catalysts exhibit better sulfur tolerance و water‑vapor resistance than some precious metal catalysts, making them promising for this application.

4.3 Resource utilization of low‑concentration coalbed methane

For low‑concentration coalbed methane in the range of 1%–3%, catalytic oxidation can convert methane into thermal energy for power generation or heating. Compared with conventional thermal oxidation, catalytic oxidation operates at a lower temperature (typically 100–200°C lower), consumes less energy, and requires lower capital investment.

5. Challenges and Outlook

Despite significant progress, several challenges remain for the broader industrial application of copper oxide catalysts in low‑concentration methane thermal catalytic oxidation:

Low‑temperature activity needs further improvement. Compared with precious metal catalysts such as Pd and Pt, CuO‑based catalysts still have inferior activity at low temperatures (<300درجة مئوية). Although precious metal catalysts offer high activity, they are expensive and resource‑constrained. How to further enhance the low‑temperature activity of CuO‑based catalysts while maintaining cost advantage is a key research direction.

Poison resistance must be strengthened. Industrial flue gases often contain sulfur compounds (على سبيل المثال, ح₂س, لذا₂) وبخار الماء, which can bind to active sites and cause catalyst poisoning. In particular, water vapor competes with methane for the same active adsorption sites, leading to severe inhibition. بالإضافة إلى ذلك, catalysts face irreversible deactivation due to high‑temperature sintering during long‑term operation.

Thermal stability requires improvement. The Tammann temperature of CuO is relatively low, making it prone to sintering under prolonged high‑temperature operation, resulting in active component agglomeration, reduced specific surface area, and consequent degradation of catalytic performance over time.

Future research directions mainly include:

• Support optimization: Selecting suitable supports (على سبيل المثال, zeolites, Al₂يا₃, CeO₂) to improve CuO dispersion and structural stability;
• Composite and doping modification: Introducing promoter elements such as Ce, الحديد, Co to construct mixed metal oxide systems with synergistic effects;
• Morphology and crystal facet engineering: Tuning the crystallite size, morphology, and exposed facets of CuO through optimized preparation methods (على سبيل المثال, sol‑gel, electrochemical oxidation) to increase the proportion of highly active facets;
• Scalable preparation processes: Developing catalyst forming processes suitable for industrial production to bridge the gap from laboratory to commercial units.

In the field of non‑precious metal catalysts, Minstrong possesses long‑standing technical expertise and product development experience in transition metal oxide catalytic materials such as copper oxide and manganese dioxide, dedicated to providing cost‑effective catalyst solutions for low‑concentration methane treatment and other industrial applications.

6. خاتمة

Copper oxide‑based catalysts, with their low cost, توافر وفيرة, and tunable catalytic properties, show promising application prospects in the thermal catalytic oxidation of low‑concentration methane. From the excellent performance of supported CuO_س/zeolite catalysts, to the synergistic enhancement of CuO‑CeO₂ composite systems, and through pilot‑scale industrial validation, CuO‑based catalysts are progressively transitioning from laboratory research to industrial practice. As non‑precious metal catalyst technology continues to advance, CuO‑based catalysts are expected to achieve broader applications in coal mine methane abatement, natural gas engine exhaust purification, and low‑concentration coalbed methane utilization, providing a practical and effective technical pathway for methane emission reduction and efficient energy use.

مؤلف: غلوريا
تاريخ:2026/8/26