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Table of Content

    12 February 2026, Volume 57 Issue 2
    RESEARCH STATUS AND PROSPECTS OF FLOW FIELD STRUCTURES IN PROTON EXCHANGE MEMBRANE ELECTROLYZERS
    2026, 57(2):  1-12. 
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    With the global advancement of carbon peaking and carbon neutrality goals, the core challenge of energy transition focuses on the efficient utilization of renewable energy sources such as wind and solar power. Proton exchange membrane (PEM) water electrolysis, characterized by its fast response, low energy consumption, and high hydrogen production pressure, is well-suited to accommodate the fluctuating nature of renewable energy generation, making it a rational choice for integrating renewable energy. However, the high cost of PEM electrolyzers (PEMEC) currently limits their large-scale application. Optimizing flow channel design to increase current density is a critical technological pathway for cost reduction. The advantages and disadvantages of parallel, serpentine, interdigitated, grid-like, and other less common flow channel typesare comprehensively reviewed,and the current state of research on the synergistic optimization of flow channels with other components (such as diffusion layers and catalytic layers) are analyzeed. Comprehensive analysis indicates that optimizing the geometric shape of flow channels can effectively improve fluid dynamic properties, enhance mass and heat transfer efficiency, while reducing flow resistance, bubble retention, and uneven local current density distribution. These improvements can significantly enhance the overall performance of the electrolyzer, providing valuable insights for the further optimization of PEMEC.
    RECENT PROGRESS IN UNDERSTANDING THE UNDERLYING SYNERGISTIC MECHANISMS OF DIATOMICCATALYSTS IN ELECTROCATALYTIC OXYGEN REDUCTION REACTION
    2026, 57(2):  13-24. 
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    The design of efficientelectrocatalystfor the oxygen reduction reaction (ORR) is crucial for advancing the practical applications of metal-air batteries and fuel cells. Diatomic catalysts (DACs) have attracted considerable interest due to their synergistic active sites, which significantly enhance the electrocatalytic ORR performance in terms of activity, selectivity, and stability.However, the exact mechanism through which these DACs achieve such synergistic enhancement remains inadequately understood.The recent advances in DACs for ORR are reviewed, with a focus on the regulation strategies that enhance catalytic performance, including the bifunctional synergistic mechanism, geometric effects, and electronic effects. These insights provide valuable guidance for the atomic-level design of efficient DACs. Furthermore, future opportunities and challenges for DACs in ORR electrocatalysis are discussed.
    DEVELOPMENT STATUS AND PROSPECTS OF LIPIDS-BASED SUSTAINABLE AVIATION FUEL PRODUCTION TECHNOLOGY
    2026, 57(2):  25-35. 
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    Under the escalating pressure for carbon emission reduction in the global aviation industry, sustainable aviation fuel, as a critical alternative to conventional aviation fuels, has seen its techno-economic feasibility emerging as a pivotal factor constraining industrial advancement. This study systematically investigates four key dimensions: the stability of lipid feedstock supply chains, hydrotreating catalysts, representative process routes, and principal economic determinants affecting sustainable aviation fuel production. It proposes breakthroughs in non-noble metal catalyst material engineering, promotes feedstock diversification and high-value utilization of by-products, thereby reducing the production costs of lipid-based sustainable aviation fuel. Furthermore, it advances the development of sustainable aviation fuel industry through establishing a “technology-economy-policy” three-dimensional synergistic system.
    ESEARCH PROGRESS ON SELECTIVE HYDROGENATION OF NITROBENZENE TO PARA-AMINOPHENOL
    2026, 57(2):  36-44. 
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    Aiming at the issues in the catalytic hydrogenation of nitrobenzene (NB) to produce p-aminophenol (PAP), such as low yield and selectivity, severe equipment corrosion, environmental pollution, and unclear technological optimization directions, this work systematically reviews the catalytic reaction mechanism, principles of regulating catalyst activity, strategies for optimizing catalyst performance, the mechanism of Bamberger rearrangement, and the influence of the medium environment on the reaction process. Analysis reveals that Pt-based catalysts exhibit excellent catalytic activity for NB hydrogenation, but the selectivity for the product PAP depends on the adsorption strength of the intermediate phenylhydroxylamine (PHA) and the reaction medium environment. The essence of catalyst modification lies in regulating the electronic structure of the metal centers to weaken their adsorption of PHA and suppress the over-hydrogenation side reaction. High selectivity for PAP can be achieved through catalyst modification methods such as doping heteroatoms, constructing core-shell structures, and forming bimetallic alloys. The properties of the support significantly affect catalyst performance, while the type of solvent and system acidity have important impacts on both hydrogenation and rearrangement reactions. Replacing sulfuric acid solutions with environmentally friendly media (CO2/H2O systems and solid acids) can prevent the generation of sulfate byproducts at the source, offering significant green advantages. Future research should focus on the holistic optimization of the medium-catalyst system, deepen the understanding of the reaction-transport coupling mechanism, and promote the practical application of green processes.
    ADVANCES IN CONTROLLED PREPARATION TECHNOLOGY OF SUGAR-BASED HARD CARBON ANODE MATERIALS FOR SODIUM-ION BATTERIES
    2026, 57(2):  45-54. 
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    Hard carbon (HC) is regarded as an ideal anode material for sodium-ion batteries (SIBs) due to its abundant closed-pore structure and large interlayer spacing. However, its practical application was limited by low initial coulombic efficiency , poor fast-charging performance and complicated preparation process. Sugar used as a common precursor of HC is easy to foam by direct high-temperature carbonization, which produces numerous open-pores, insufficient closed-pore volume and uneven distribution, which in turn affects Na+ storage performance. To solve these problems, preparation strategies including hydrothermal, pre-oxidation, molecular cross-linking and template methods have been adopted to increase interlayer spacing and closed pore volume of sugar-based HC materials, for enhancing Na+ storage performance. This review summarizes in detail the related technologies for the preparation of sugar-based HC anode materials. Subsequently, the preparation problems and research focusing on the sugar-based HC materials have been rosed, and a new controllable preparation method of high-performance HC anode materials in SIBs also has been proposed in the further.
    RESEARCH PROGRESS ON HIGH-ENTROPY CATHODE MATERIALS FOR SODIUM-ION BATTERIES
    2026, 57(2):  55-61. 
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    Sodium-ion batteries have emerged as a crucial option for next-generation energy storage systems owing to their cost advantage. However, this system still confronts numerous challenges, such as poor cycle stability, phase transitions, and structural degradation. Among various modification methods, the high-entropy strategy exhibits remarkable advantages due to its unique compositional and structural characteristics. Researchers have gradually applied the high-entropy strategy to sodium-ion battery materials to enhance their electrochemical performance. Focusing on three types of cathode materials—layered transition metal oxides, polyanionic compounds, and Prussian blue analogs—this paper reviews the positive impacts of the high-entropy strategy on material structural stability, phase transition suppression, and ion diffusion kinetics. It also summarizes the current application status and key challenges of high-entropy materials in sodium-ion batteries, and puts forward prospects for future research directions.
    RESEARCH PROGRESS ON CATALYTIC SYSTEMS FOR PROPANE DEHYDROGENATION TO PROPYLENE
    2026, 57(2):  62-67. 
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    Against the backdrop of continuously growing global propylene demand and the drive toward carbon neutrality, propane dehydrogenation (PDH) has emerged as a key route for propylene production due to its significant energy-saving advantages. In recent years, critical breakthroughs have been achieved in both catalyst design and reaction engineering: Pt-based catalysts achieve high selectivity and long-term stability through dynamic active site regulation; the zeolite confinement strategy effectively suppresses sintering; non-noble metal Co-based catalysts maintain high activity while reducing costs. In terms of reaction engineering, the chemical looping oxygen supply coupled with hydrogen combustion technology has broken through the thermodynamic equilibrium limitation, enabling efficient energy recycling, and intelligent integrated processes have significantly reduced carbon emissions. Future efforts should focus on directions such as multiscale simulation, reactor-catalyst synergistic design, and green electricity coupling to promote the development of PDH technology towards low carbonization and high performance, thereby supporting the green transformation of the olefin industry.
    CURRENT RESEARCH AND APPLICATIONS OF FREEZING PROCESS FOR WATER TREATMENT
    2026, 57(2):  68-76. 
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    As a green, low-energy water treatment approach, the freezing process has attracted growing attention in recent years for high-salinity organic wastewater treatment and resource recovery. This paper systematically reviews the mechanisms of physical separation and freeze-induced chemical acceleration, summarizes the development status of mainstream processes such as progressive freeze concentration (PFC) and suspension freezing (SFC), and elucidates the latest advances in external-field-assisted freezing processes. Building on this, we provide an in-depth analysis of the efficiency and mechanisms by which the freezing process accelerates chemical reactions to mitigate heavy-metal toxicity and remove organic contaminants. Finally, we evaluate the engineering application potential of the freezing process in industrial wastewater treatment, seawater desalination, and sludge management. In the context of the “dual-carbon” goals of carbon peaking and carbon neutrality, future work should prioritize the development of low-carbon refrigeration systems and the exploration of green, intelligent freezing-process technologies to enable efficient purification and resource-oriented utilization of industrial wastewater.
    RESEARCH PROGRESS ON SMART RESPONSIVE MEMBRANES IN OIL-WATER SEPARATION
    2026, 57(2):  77-89. 
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    In recent years, the rapid development of global industry has led to a large discharge of oily wastewater, which poses a serious threat to human health, ecosystems and socio-economy. Among the many treatment technologies, membrane separation method is widely used due to its advantages of simple operation and low energy consumption, but traditional membranes still face multiple challenges when treating of oily wastewater: First, its fixed surface wettability (such as single superhydrophilic or superhydrophobic properties) is difficult to adapt to different types of oil-water mixtures; second, the non-adjustable pore size of traditional membranes leads to limited separation selectivity; third, oil pollution easily causes membrane pore blockage and surface contamination, resulting in a rapid decline in the flux of traditional membranes. As a new functional material, the intelligent response membrane can dynamically regulate the wettability and pore size of the membrane surface by sensing environmental stimuli, which can achieve selective separation of oil or water phase, significantly improve the separation efficiency and adaptability of different types of oil-water emulsions, and has the ability to resist pollution and self-cleaning, and can simultaneously achieve high throughput and high rejection rate, which has become a research hotspot in recent years. In this paper, the mechanism and performance characteristics of intelligent response membranes are systematically expounded, and the types of stimulus responses (pH-responsive, temperature-sensitive, photo-sensitive, magnetic-responsive, etc.) are classified and reviewed, focusing on the analysis of their technological breakthroughs and application progress in the field of oil-water separation, and the future development direction is proposed for the limitations of existing technologies.
    STATUS OF TAR TREATMENT TECHNOLOGIES AND THEIR INFLUENCE ON OVERALL CONFIGURATION OF SAF PRODUCTION
    2026, 57(2):  90-95. 
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    Under the background of "Carbon peaking and Carbon Neutrality", the emission reduction of aviation industry can be achieved by blending withSustainable Aviation Fuels (SAF). In the SAF production route, the technology of biomass gasification synthesis to SAF has been widely concerned around the world in recent years for its advantages such as feed adaptability. However, moving bed or fluidized bed biomass gasification technology will produce tar much more difficult to remove than similar gasification technologies, which will have a great impact on the long-term operation and economic benefits of the plant. This article reviews the tar treatment technology in the production of SAF from biomass gasification, and studied the impact of different tar treatment technologies on the overall configuration. By comparing the advantages and disadvantages of different tar treatment technologies, the role of these technologies in the overall configuration is studied. Finally, the technical route and tar treatment technology are summarized and prospected, and targeted suggestions are put forward in order to provide new ideas for the overall process planning of biomass gasification to SAF in the future.
    PROGRESS ON HYDROGEN PRODUCTION BY STEAM REFORMING OF GLYCEROL
    2026, 57(2):  96-103. 
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    Glycerol steam reforming represents a pivotal technological pathway for the value-added utilization of glycerol, a by-product of biodiesel production, and for the generation of green hydrogen. The industrial application of this reaction centers on the development of catalysts that exhibit high activity, high selectivity, and superior stability. This paper systematically reviews recent research progress in catalyst design for hydrogen production by glycerol steam reforming, focusing on the three key aspects: active metals, supports, and promoters. It provides an in-depth analysis of the construction of catalyst active sites, metal-support interactions, and the regulatory mechanisms for enhancing resistance to coking and sintering. Finally, it analyzes the theoretical and technical challenges currently facing catalyst design and outlines future development directions.
    RESEARCH PROGRESS ON RESOURCE RECOVERY AND UTILIZATION OF NOx FROM SPENT NUCLEAR FUEL REPROCESSING OFF-GAS
    2026, 57(2):  104-111. 
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    The tail gas with high-concentration of nitrogen oxides (NOx) produced during the spent fuel retreatment process in the nuclear power industry is not only a key target for the control of radioactive pollutants but also a nitrogen resource with recycling value. This paper systematically reviews the key links of the NOx recovery technology system in the post-treatment scenario: Firstly, the removal methods for characteristic radioactive impurities in the exhaust gas, especially fission products such as ruthenium-106; Secondly, the drying process of nuclear-grade tail gas was summarized, emphasizing the significance of deep drying (dew point < -70℃) for the subsequent separation system. The energy efficiency and applicable scenarios of solvent absorption, deep condensation dehydration, adsorbent adsorption, and membrane separation were compared. Furthermore, the core technologies for NOx enrichment and separation were elaborated in detail, including the low-temperature absorption method with nitric acid solution (0—5℃) and the selective adsorption of zeolite adsorbents. The industrial value of these two methods in the preparation of high-purity liquid N2O4 (purity >99.9%) was pointed out, providing technical support for the safe disposal and resource utilization of tail gas from spent fuel after-treatment. In the future, it is necessary to focus on developing new separation materials that are resistant to acid and radiation aging to enhance the economic efficiency and stability of the process.
    HYDRODYNAMIC CHARACTERISTICS OF MICROBUBBLES IN GAS-LIQUID-SOLID FLUDIZED BED
    2026, 57(2):  112-123. 
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    Gas-liquid-solid fluidized beds (GLSFB) are widely used in various fields due to their excellent interphase mixing and superior mass and heat transfer. However, the gas-liquid phase interface area of millimeter-scale bubbles is small, resulting in low transfer efficiency. In contrast, the specific surface area of microbubbles has the advantage of a significant increase of several orders of magnitude. Introducing microbubbles into GLSFB can significantly enhance the mass and heat transfer rates and prolong the residence time. Focusing on the hydrodynamic characteristics of the microbubble-liquid-solid three-phase fluidized bed, and based on telecentric imaging technology, the influence law of operating parameters on the multiphase flow behavior is explored. Based on Python programming, combined with telecentric camera and manual correction algorithms, the rapid measurement and calculation of three-phase flow parameters were achieved. The results show that the Sauter diameter of microbubbles and the local gas holdup increase with the increase of the apparent gas velocity, and first increase and then decrease with the increase of the apparent liquid velocity of the main water flow. The solid content rate of the large particle system decreases with the increase of gas velocity, while the change in the small particle system is not obvious.
    ELECTRO-REGULATED SUPERLUBRICITY BEHAVIOR AND MECHANISMS OF BLACK PHOSPHORUS NANO-ADDITIVES
    2026, 57(2):  124-133. 
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    A composite lubricating solution was prepared using polyethylene glycol (PEG) as the base oil and black phosphorus (BP) nanosheets as additives. The tribological behavior of the composite solution on steel surfaces under electrical signal stimulation was investigated, along with the influence of multiple factors on friction. Compared to tests without electrical stimulation, negative electrical stimulation significantly reduced the coefficient of friction (COF), while positive stimulation caused a notable increase in COF. under the conditions of -0.25 V voltage,BP concentration of 25~100 μg/g, normal load of 2~4 N, and sliding speed of 100 mm/s, the composite solution achieved macroscale superlubricity on steel surfaces. The worn surfaces were analyzed using scanning electron microscopy (SEM) and X-ray photoelectron spectroscopy (XPS). The results indicate that the superlubricity mechanism under negative electrical stimulation primarily arises from the synergistic effects of three factors: the electrically induced full oxidation of BP to form a POx-containing tribochemical reaction film, a PEG adsorption film, and a PEG fluid film. This study demonstrates the feasibility of achieving macroscale superlubricity on steel interfaces via electrical stimulation, thereby laying the foundation for the practical application of superlubricity technology in engineering environments.
    SIMULATION OF FLUID FLOW CHARACTERISTICS IN FIXED BEDS WITH CATALYST PARTICLES OF DIFFERENT SHAPES
    2026, 57(2):  134-145. 
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    Fixed-bed reactors are widely used in chemical production, and the shape of the catalyst particles can significantly influence the fluid flow characteristics within the bed. Using a DEM-CFD one-way coupling approach,the fluid flow patterns in catalyst beds packed with spherical, cylindrical, trilobe, and butterfly-shaped catalyst particles were investigated. Results demonstrate that increased inlet velocity induces flow complexity. Vortices were observed in all four types of particle beds, while channeling flow was notably present in beds with spherical and cylindrical particles. The butterfly-shaped catalyst bed exhibited the most uniform fluid velocity distribution. The pressure drop calculated by the Ergun equation showed good agreement with the simulated values for spherical and cylindrical particle beds, but exhibits significant deviations for trilobe and butterfly-shaped particle beds. A modified Ergun model incorporating shape-dependent correction factors achieved prediction accuracy within 5% for trilobe and butterfly-shaped particles. Additionally, the spherical particle bed demonstrated the shortest average residence time, while the cylindrical, trilobe, and butterfly-shaped particle beds exhibited similar average residence times. These findings are expected to provide valuable insights for the optimization of particle structures in fixed-bed reactors.
    PREPARATION OF METAL-ENCAPSULATED SILICALITE-1 ZEOLITE AND ITS ADSORPTION PERFORMANCE FOR ACETONE
    2026, 57(2):  146-157. 
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    Conventional silicalite-1 (S-1) zeolite exhibits limited efficiency in adsorbing polar volatile organic compounds molecules (e.g., acetone) due to its scarcity of acid sites. Based on this, a series of metal-encapsulated S-1 zeolites were prepared by introducing metals Ag, Cu, Fe, and Ni into S-1 via in-situ synthesis. Systematic characterization and acetone adsorption performance tests were conducted on both S-1 and the metal-encapsulated S-1 zeolites. The results show that Fe@S-1 exhibits the best acetone adsorption performance, with its acetone adsorption breakthrough capacity increasing by approximately 10% compared to that of S-1. This improvement is attributed to the introduction of Fe, which significantly enhances the microporous specific surface area and the number of Lewis acid sites in S-1. As the Fe loading increases, the number of Lewis acid sites in Fe@S-1 shows an upward trend, and the crystal grains gradually decrease in size, forming aggregated particles with intercrystalline mesopores. These characteristics not only enhance the adsorption of acetone on Fe@S-1 but also reduce the diffusion resistance of acetone, thereby improving its adsorption capacity for acetone. The fitting results of the adsorption kinetic model indicate that the adsorption behavior of acetone on Fe@S-1 is governed by both physisorption and chemisorption, with intraparticle diffusion playing a dominant role in the adsorption process.
    EFFECT OF ALUMINUM SOURCE TYPE ON ALUMINUM ATOM DISTRIBUTION AND BUTENE CRACKING REACTION PERFORMANCE OF ZSM-5 ZEOLITE
    2026, 57(2):  158-165. 
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    In this study, ZSM-5 zeolites were synthesized via the hydrothermal method using sodium metaaluminate,sodium hydroxide,pseudo-boehmite and aluminum isopropoxide as aluminum sources, respectively. Based on the characterization of physicochemical properties and the catalytic performance test of butene cracking, the effect of aluminum source types on the sitting of framework aluminum atoms and structure-activity relationship was investigated. The results showed that the type of aluminum source had little influence on the crystal structure, pore structure, surface morphology, and total acid amount of ZSM-5 zeolite. However, it exerted a significant effect on the distribution of framework aluminum atoms. In the research synthesis system, aluminum sources with higher solubility (e.g., sodium metaaluminate) compared to those with slower hydrolysis rates (e.g., pseudoboehmite and aluminum isopropoxide), the proportion of aluminum atoms located in the straight channels (α-sites) is increased. Due to spatial restriction, zeolites with a high proportion of framework aluminum atoms located at α-sites exhibit high propylene selectivity in butylene catalytic cracking reaction.This study not only verified the structure-activity relationship between the acid site distribution of ZSM-5 zeolites furtherly, and also provided a basis for the directional synthesis of high-performance catalyst for butylene catalytic cracking.
    INFLUENCE OF METAL CATION VALENCE STATE ON ELECTRICALLY REGULATED FRICTION BEHAVIOR
    2026, 57(2):  166-173. 
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    This study investigates the influence of metal cation valence state on electrically regulated friction behavior using three inorganic salts with distinct valence state—NaCl, MgCl2, and LaCl3—as lubricant additives. Friction tests reveal that the monovalent Na+-based lubricant exhibits significant friction modulation under negative electrical stimulation, with the friction coefficient decreasing from 0.085 (at 0 V) to 0.028 (under negative voltage), representing a 67% reduction. In contrast, divalent Mg2+ and trivalent La3+ ions show no comparable friction-regulation capability. The morphological features, surface roughness, and chemical states of wear scars were analyzed using white light interferometry, scanning electron microscopy, and X-ray photoelectron spectroscopy. The results demonstrate that the friction-regulation mechanism of monovalent Na+ ions under negative voltage arises from enhanced adsorption on the steel ball surface, thereby improving anti-friction performance. Conversely, the adsorption capacities of Mg2+ and La3+ ions remain unaffected by electrical signals, leading to negligible changes in their friction-reduction properties.
    Pt/C-CATALYZED SELECTIVE OXIDATION OF ETHYLENE GLYCOL TO GLYCOLIC ACID
    2026, 57(2):  174-181. 
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    The selective oxidation of ethylene glycol (EG) to glycolic acid (GA) under ambient pressure constitutes a crucial process for building a green carbon cycle and synthesizing value-added chemicals. This study employed a Pt/C catalytic system to systematically investigate the effects of reaction temperature, oxygen partial pressure, and types of reaction promoter on the reaction performance. The results indicate that the optimal reaction temperature ranges from 60 to 80 °C, with an apparent activation energy of 11.27 kJ/mol. A high GA selectivity of 90% was achieved, and the reaction order with respect to oxygen was determined to be only 0.24, confirming that highly efficient catalysis can be realized under mild positive oxygen pressure. Furthermore, a semi-continuous mild positive-pressure reaction system achieved a GA selectivity of 70%. Screening of reaction promoters revealed that the introduction of ascorbic acid significantly enhanced both reaction conversion and selectivity [with a conversion rate of 46% and total selectivity for glycolaldehyde (GD) and GA reaching 100%]. In contrast, quinone-based promoters, while facilitating active oxygen transport, showed limited improvement in conversion. In situ infrared spectroscopy analysis elucidated the tandem reaction pathway, wherein EG is converted to GA via a GD intermediate.
    RESEARCH ON THE HEAT DISSIPATION EFFECT OF CROSS-SHAPED ELECTRONIC COMPONENTS WITH PHASE CHANGE AND LIQUID COOLING COUPLING METHOD
    2026, 57(2):  182-189. 
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    To improve the heat dissipation efficiency and uniformity of cross-shaped electronic components, this study investigated the thermal performance of composite phase-change materials (PCM) consisting of copper oxide (CuO) or graphene nanoplatelets (GNP) mixed with paraffin wax, as well as the effect of nanoparticle content on heat dissipation. The cooling methods and temperatures were varied to compare their cooling performance. The results show that higher CuO or GNP content in the composite PCM leads to improved heat dissipation efficiency. When the volume fraction of CuO or GNP reaches 2%, the heat dissipation efficiency of CuO/paraffin and GNP/paraffin composite PCMs increases by 69.81% and 157.14%, respectively, compared to pure paraffin.Furthermore, the study examined the cooling performance of coupled phase-change heat dissipation with different liquid cooling methods. The results indicate that immersion liquid cooling provides better heat dissipation uniformity than single-wall cooling plate methods. For the GNP/paraffin composite PCM-immersion liquid cooling coupled system, higher graphene content and lower cooling temperatures lead to improved heat dissipation efficiency. When the cooling temperature decreases from 304 K to 302 K, the cross-shaped electronic component exhibits the maximum temperature drop of 0.83 K.
    NUMERICAL SIMULATION OF HEAT TRANSFER PERFORMANCE OF SOLID OXIDE ELECTROLYSIS CELL FEEDSTOCK ELECTRIC HEATER ENHANCED BY FOAM METAL
    2026, 57(2):  190-199. 
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    Solid oxide electrolysis cell is a key technology for green hydrogen production, but its feedstock electric heater has the problems of low convective heat transfer efficiency and large volume, which restricts its commercial application. In order to improve the compactness and efficiency of the heater, this study proposes to fill the opening foam metal in the flow channel to enhance heat transfer. The effects of foam hole parameters and foam fin combination on flow, heat transfer and pressure drop are analyzed through numerical simulation. The results show that increasing the inlet flow rate leads to a quadratic increase in pressure drop and a logarithmic increase in convective heat transfer coefficient; The foam structure with high porosity and high pore density has better heat transfer effect. Because of its large specific surface area and complex flow channel, it can destroy the thermal boundary layer and significantly enhance convection, but its thermal conductivity is still inferior to that of fins. The foam fin composite structure makes comprehensive use of the high thermal conductivity of the fins and the strong convection disturbance of the foam, significantly improving the wall heat conduction and the overall heating temperature of the fluid, and effectively enhancing the performance of the electric heater.
    EXPLORATION AND PRACTICE OF DEEP UTILIZATION OF WASTE HEAT IN PETROCHEMICAL ENTERPRISES UNDER THE DUAL CARBON GOALS
    2026, 57(2):  200-206. 
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    This paper provides an in-depth analysis of the challenges faced by China's petrochemical industry under the "Dual Carbon" goals, emphasizing that improving energy efficiency is an essential pathway to achieve these targets. Through a case study on the deep utilization of low-temperature waste heat in a petrochemical enterprise of China National Offshore Oil Corporation (CNOOC), the study systematically examines the technical principles, implementation methods, and economic benefits. The findings offer both theoretical foundations and practical references for the advanced utilization of waste heat in petrochemical plants.
    ANALYSIS OF PROPERTIES COMPOSITION AND STRUCTURE OF FCC SLURRY
    2026, 57(2):  207-212. 
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    Fluid catalytic cracking(FCC) slurry as the by-product of the FCC process, can be used to prepare high-end functional carbon materials. It is of great significance to analyze its properties and structural characteristics for further processing and high-value-added utilization. Based on the investigation of basic properties and compositions, the structure of the slurry was characterized by NMR, FTIR, SEM, XRD, and a laser particle size analyzer. The average structural parameters were calculated by the improved Brown-Ladner method. The results show that slurry has the characteristics of high density, high viscosity, and high solid content. The ash content is 0.49%, the aromatic content is 69.48%, the H/C atom ratio is 1.07, and the average molecular structure is acondensed aromatic ring systemwith3.01 rings. The solid particles in theslurry are irregular in shape and formed from the aggregation of molecular sieve catalyst powder. The particle size is mainly distributed in 1—10μm.
    PRODUCTION OF 5-HYDROXYMETHYLFURFURAL FROM GLUCOSE CATALYZED BY IM-5 ZEOLITE
    2026, 57(2):  213-220. 
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    This study investigates the catalytic performance of ZSM-5 (MFI), IM-5 (IMF), and oxalic acid-treated IM-3M zeolites in the conversion of glucose to 5-hydroxymethylfurfural (HMF). The physicochemical properties of the zeolites were systematically characterized by XRD, SEM,BET, NH3-TPD, and Py-FTIR. The results show that both IM-5 and IM-3M zeolites exhibit larger specific surface areas (412.1 m2/g and 459.5 m2/g, respectively) than ZSM-5 (371.9 m2/g). Moreover, the IM-3M sample obtained after oxalic acid treatment possesses more mesopores, leading to a significant increase in total pore volume (0.62 cm3/g), enhancing the diffusion of substrates and products. The reduction acid strength of IM-3M further suppressed coke formation, resulting in superior performance in the glucose-to-HMF conversion.Consequently, the IM-3M catalyst exhibited superior performance in a THF/NaCl-H2O biphasic system, achieving 95.0% glucose conversion with 59.2% HMF selectivity at 170 ℃ within 60 min. After four consecutive reaction cycles, the HMF selectivity remained above 50%, and the zeolite structure showed no significant changes, demonstrating excellent catalyst stability.
    EFFECT OF LANTHANUM DOPING CONTENT ON MATHANE REDUCTION KINETICS FOR IRON-BASED OXYGEN CARRIER DURING CHEMICAL LOOPING PROCESSES
    2026, 57(2):  221-230. 
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    To investigate the influence mechanism of metal doping contenton the reduction kinetics of iron-based oxygen carriers,a series of iron-based oxygen carriers with low concentration lanthanum doping (molar fraction of lanthanum : 0 - 3%) were synthesized, the structureof iron-based oxygen carriers with different lanthanum doping loadings were examined by X-ray diffraction, N2 adsorption-desorption, scanning electron microscopy, etc., and the variation trends of methane reduction reaction kinetics were evaluated through a coupled approach of modelling calculations and experiments. Results indicate that the doped lanthanum enters the lattice of iron-based oxygen carrier, causing leftward shifts in the XRD diffraction peaks of Fe2O3 and ZrO2. Moreover, the degree of shift increases with increasing lanthanum doping concentration. At a lanthanum molar fraction of 3%, a distinctive perovskite-structured LaFeO3 crystalline phase forms, leading to a decrease in the specific surface area of oxygen carrier. The methane reduction reaction over iron-based oxygen carriers comprises three steps: Fe2O3 → Fe3O4 (R1), Fe3O4 → Fe1-xO (R2), and Fe1-xO → Fe (R3). Steps Rand Rconform to first-order reaction models, while R3 follows a nucleation model. Lanthanum doping does not alter the methane reduction reaction pathway or its kinetic model of oxygen carrier. The 1% La-doped oxygen carrier exhibits an optimal reduction performance, significantly enhancing the overall reaction rate and simultaneously lowering the activation energies of each reaction step.