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The Chinese Journal of Process Engineering 2025 Vol.25
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The Chinese Journal of Process Engineering 2025, 25 (1): 0-.
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Design and preparation of targeted drug loading systems for treatment of Alzheimer's disease
Jiayuan QIU Xi CHEN Xiaoqian YE Lilong ZHOU Jimmy YUN
The Chinese Journal of Process Engineering 2025, 25 (1): 1-19. DOI:
10.12034/j.issn.1009-606X.224086
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Alzheimer's disease (AD) is a very common progressive and destructive degenerative disease of the central nervous system that affects the quality of life of the elderly and poses a serious risk to their lives, placing a huge economic burden on families, society and the state. There are not many breakthroughs as well as innovations in current medications for the treatment of AD, and there is also the challenge of breaking through the blood-brain barrier, and improper treatment may lead to adverse reactions in patients. Targeted drug delivery system, as an effective therapeutic modality, can significantly reduce the concentration of drugs in the blood, the frequency of drug delivery and the drug toxicity, while increasing the concentration and efficacy of drugs at the target site and drug bioavailability, as well as providing a slow-release effect for drugs. In addition, the targeted drug delivery system is also expected to penetrate the blood-brain barrier, improve blood-brain penetration, realize brain targeting, and deliver drugs precisely, thus providing an efficient and safe way to treat AD. This work reviews the pathogenesis of AD, the non-pharmacological methods of adjuvant drug therapy for the treatment of AD as well as the mechanism of action and side effects of the main drugs targeting amyloid β protein (Aβ) aggregation, acetylcholinesterase inhibition, and receptor antagonism, etc. It also briefly introduces and combs through as well as summarizes the targeting drug delivery systems for the treatment of AD such as magnetic nanoparticles, liposomes, and so forth, points out the problems that exist at the moment, puts forward the possible solutions, and indicates the direction of possible development in the future.
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Study of ammonium salt crystallization behavior in high pressure heat exchanger of hydrogenation unit
Jianwen ZHANG Guoqing SU Leilei FENG Yan LI Fan ZHANG Shilin LU Yahui ZHAO Gang SHENG
The Chinese Journal of Process Engineering 2025, 25 (1): 20-33. DOI:
10.12034/j.issn.1009-606X.224129
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The problem of ammonium salt crystallization is very important for the safe production of the heat exchange system in hydrogenation plant, which often leads to blockage, corrosion leakage, and unplanned shutdown of the heat exchange system. It is of great significance to the study of the crystallization process and distribution characteristics of ammonium salt. In order to explore the problem of ammonium salt corrosion failure in the high pressure heat exchanger of diesel hydrogenation plant, the ammonium salt crystallization temperature was determined based on the concentration of components, and the C++ ammonium salt crystallization model and user-defined function (UDF) were written. Through isoparametric modeling of the heat exchanger, numerical simulations of the multiphase flow field, heat and mass transfer processes were carried out using ANSYS Fluent finite element analysis software and embedded UDF to analyze the intrinsic causes of corrosion failure. The mechanism of ammonium salt crystallization can be divided into heat transfer control and mass transfer control. The simulated ammonium chloride crystallization corrosion location and the actual corrosion coincided. The significant factors that influence the ammonium salt crystallization can be get through the orthogonal experimental analysis. The independence of the significant factors were analyzed to get the specific impact on the ammonium salt crystallization. Further, it provides a basis for the optimization of process device operation.
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Multi-objective parameter identification method for methanation reaction kinetics combined with process simulation
Zhuohang JIN Xiaoxia HAN Fengyi LIU
The Chinese Journal of Process Engineering 2025, 25 (1): 34-43. DOI:
10.12034/j.issn.1009-606X.224091
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The simulation model of the methanation reactor can guide the optimization of the methanation process, which is of important research significance. However, the construction of the methanation reactor simulation model involves two parts: reactor modeling and reaction kinetics modeling, and the two models are coupled with each other. Neglecting the reactor transferring role and considering the kinetic model alone or solving the reactor model from the chemical equilibrium point of view without focusing on the kinetics will lead to low simulation accuracy, which makes it difficult to guide the optimization of the process effectively. The multi-objective optimization algorithm is used to identify the kinetic parameters of the methanation reactor model built in Aspen Plus, which can achieve high-precision identification of the parameters of the kinetic equation set with fewer data points, and the method can effectively solve the problem of identifying the parameters of the kinetic equation set in the complex reaction process by considering the reactor action and reaction kinetics at the same time. The results show that the multi-objective parameter identification method of the methanation reactor process simulation model can reduce the root-mean-square errors of CO conversion and CH4 selectivity simulation results to 1.96% and 4.59%, respectively, which are lower than those of the existing kinetic models.
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Preparation and characterization of abrasion-resistant core-shell alumina support used in fluidized bed reactors
Yinhu ZHANG Zhanguo ZHANG Guangwen XU
The Chinese Journal of Process Engineering 2025, 25 (1): 44-52. DOI:
10.12034/j.issn.1009-606X.224170
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The Ni-based catalyst used in fluidized bed methane dry reforming reaction needs to have both high abrasion resistance and high activity, which requires the catalyst support itself to have both good abrasion-resistance and high Ni loading capacity. Based on the phase transformation mechanism of Al2O3, this study aims to prepare a type of core-shell @Al2O3 support with its shell in abrasion-resistant α-phase and its core in porous γ- or θ-phase Al2O3 through calcination of γ-Al2O3 at high temperatures. For this purpose, commercially available mesoporous γ-Al2O3 particles with a specific surface area of 325 m2/g and an average particle size of 850 μm were used as precursor material and calcinated in a vertical high temperature furnace at different temperatures for different periods of time. For prepared @Al2O3 samples, X-ray diffraction (XRD) analysis and N2 isothermal adsorption-desorption measurement were performed to characterize their phase transformation degree; electron microscopy (SEM) observation of their particles' cross-sections was conducted to confirm the formation of core-shell structure. And cold- and hot-state fluidized bed abrasion tests were carried out to evaluate their abrasion-resistance. The XRD results obtained have shown that the target core-shell @Al2O3 support can be prepared by calcination of porous γ-Al2O3 particles at 1250, 1300, and 1370℃ for different periods of time. SEM and BET characterization results also confirmed that the core-shell @Al2O3 particles with a shell thickness of 30~50 μm, a specific surface area of 86 m2/g and an average pore size of 22 nm were successfully prepared by calcination at 1300℃ for 6 min. The results of the fluidized-bed abrasion tests further confirmed that this core-shell @Al2O3 had the same excellent abrasion resistance as α-Al2O3, and the rate of its weight loss by abrasion at 800℃ was only 0.003wt%/h. At last, with this core-shell @Al2O3 as support, 10wt%Ni@Al2O3 catalyst was prepared in an impregnation approach and its abrasion resistance was evaluated at 800℃ to confirm that it also had the same resistance as α-Al2O3, which strongly suggests that such @Al2O3 supported catalyst has a good application prospect in fluidized bed reactor systems.
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Mechanism analysis of COSMO-RS screening ionic liquid to separate isopropanol-acetonitrile
Jungang FAN Yue MENG Mingxin HE Jiarui HAO Wenxiu LI
The Chinese Journal of Process Engineering 2025, 25 (1): 53-61. DOI:
10.12034/j.issn.1009-606X.224115
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The efficient separation of alcohol-nitrile azeotropes produced in chemical production is a difficult problem in the chemical industry, and the widely used extractive distillation techniques in this field have put forward further requirements for the selection of extractants and mechanism analysis. The COSMO-RS model can be used to predict the thermodynamic properties of the fluid through quantitative calculation, and select the ionic liquids (ILs) extractant agent suitable for a certain system from a large number of possible solvents, which can significantly reduce the experimental amount and enhance the research efficiency. By comparing the model prediction value with the experimental value, the accuracy of the COSMO-thermX software in predicting the separation of alcohol and nitrile azeotropes by ionic liquid has been verified. Based on the COSMO-RS model, with the separation selectivity of ILs, the influence of ILs on the relative volatility of isopropyl alcohol (IPA)-acetonitrile (MeCN) near boiling point and the solubility of ILs to IPA as indexes, the effects of 456 ILs composed of 24 cations and 19 anions on the separation of IPA-MeCN azeotrope were calculated and analyzed. The results showed that ammonium tetraethylacetate ([N2,2,2,2][Ac]) was the best extractant. The interaction between IPA-MeCN molecules in the mixture and [N2,2,2,2][Ac] was studied by means of excess enthalpy analysis, interaction energy analysis and weak interaction analysis, and the separation mechanism of [N2,2,2,2][Ac] as an extractant for separating IPA-MeCN at molecular level was discussed, and the results showed that the interaction between [N2,2,2,2][Ac] and IPA was stronger than that with MeCN, thereby accelerating the disruption of the original azeotropic structure. The assistance of the COSMO-RS model in screening ILs extractants and analyzing separation mechanisms provided important information for further understanding the function of ionic liquid in azeotropic system separation, and had important reference value for the development of novel extractive distillation technologies.
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Mechanism and kinetics of alkaline leaching for low-grade bauxite activated by pre-roasting
Tianxiang CHEN Haijun MA Kaifeng PANG Yuantao WANG Yifei ZHANG
The Chinese Journal of Process Engineering 2025, 25 (1): 62-69. DOI:
10.12034/j.issn.1009-606X.224137
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In recent years, as the production of alumina in China has sharply increased, the available high-quality bauxite resources have fallen short for alumina in China. Meanwhile, the amount of low-grade bauxite resources, i.e., containing high-sulfur and carbon, with a low aluminum-to-silicon ratio, is underused due to the lack of available technology. The depletion of high-quality bauxite resources and the utilization problem of low-grade bauxite ores have become the main bottlenecks restricting the sustainable development of the alumina industry in China. Therefore, the effective utilization of low-grade bauxite resources is of great significance for the sustainable development of the alumina industry in China. To solve this issue, the present study employed a potential process of sodium nitrate pre-roasting activation coupled with leaching in low-alkali solution for low-grade bauxite. The bauxite and pre-roasted clinker were characterized by scanning electron microscopy (SEM), X-ray diffraction (XRD), etc. The effects of technical parameters such as the temperature of pre-roasting bauxite alkali leaching, leaching time, and solid-liquid ratio on the leaching of alumina were studied in detail, focusing on the mechanism and kinetics of low-alkali leaching of pre-roasted bauxite. The results showed that after pre-roasting with sodium nitrate, the microstructure of the bauxite became loose, exhibiting a porous and grooved structure. Under the appropriate leaching conditions with a solid-to-liquid ratio of 300 g/L, using a lower concentration of caustic soda solution 160 g (Na2O)/L compared to the traditional Bayer process for 60 minutes at 270℃, 87.22% alumina of the pre-roasted bauxite with an original aluminum-to-silicon ratio of 3.57 was leached, and the aluminum-to-silicon ratio of red mud reduced to 0.88. This method could effectively improve the leaching rate of alumina in the bauxite and overcome the limitation of the theoretical leaching rate of Bayer process. The apparent activation energy for the leaching of alumina in the pre-roasted bauxite was regressed as 23.21 kJ/mol, the leaching process was controlled by mixed mechanisms.
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Effect of annealing on microstructure and mechanical properties of cold-rolled 430 ferritic stainless steel
Shuaikang XU Xiaoyu SUN Lin CHEN Jinghui LI Mingya ZHANG
The Chinese Journal of Process Engineering 2025, 25 (1): 70-79. DOI:
10.12034/j.issn.1009-606X.224124
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After cold-rolled deformation of 430 ferritic stainless steel at room temperature with a 55% reduction, the annealing treatments were carried out at 800, 850, 900, 950, and 1000℃ for 15 min, followed by in?situ tensile and nanoindentation tests. The microstructure and mechanical properties of 430 ferritic stainless steel were studied by field emission scanning electron microscopy (SEM), electron backscattering diffraction (EBSD) and transmission electron microscopy (TEM). The results indicated when the annealing temperature increased from 800 to 850℃, the recrystallization proportion of the cold-rolled microstructure of the sample gradually increased, the recrystallization proportion increased from 66% to 68%, and the average grain size decreased significantly, from 9.23 μm to 8.07 μm. At this time, the microstructure of the sample was mainly affected by grain refinement, and the strength and plasticity of the sample were improved to a certain extent. The hardness also showed a certain degree of improvement. When the annealing temperature increased from 900℃ to 1000℃, the recrystallization ratio of the cold-rolled specimens increased from 71% to 89%, the average grain size increased by about 1.5 times, the dislocation density decreased significantly, the strength of the specimens decreased while the plasticity increased, and the hardness decreased significantly. When the sample was annealed at 850℃, the grain size in the structure is small and uniform, the yield strength reached 882 MPa, the elongation reached 17.5%, and the hardness value wass 2.08 GPa, indicating good microstructural and mechanical properties. Therefore, the optimal annealing process of 430 ferritic stainless steel was held at 850℃ for 15 min.
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Evolution of cementite in high strength pearlitic steel wires during drawing
Yan WU Jianyu JIAO Fengmei BAI Hongwei ZHOU Gang ZHAO Jun XUE Guangwen ZHENG
The Chinese Journal of Process Engineering 2025, 25 (1): 80-88. DOI:
10.12034/j.issn.1009-606X.224150
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Cold-drawn pearlitic steel wire is widely used because of its high strength and certain toughness. In the process of cold drawing, the evolution of cementite lamellae has an important influence on the strength and toughness of steel wire. In this work, high-carbon steel wire rod with a diameter of 7.81 mm is selected, and the series of high-strength pearlite steel wires with different diameters are obtained by multi-pass cold drawing until the maximum true strain reached to 2.18. The evolution law and microscopic mechanism of cementite lamellae evolution during cold drawing are observed by transmission electron microscope (TEM) and scanning electron microscope (SEM) methods. The results show that during steel wire drawing, the longitudinal fibrous pearlite structure becomes more obvious with the increase of strain, and pearlite lamellae composed of ferrite and cementite are gradually adjusted to the drawing direction, and all of them are parallel to the drawing direction at the strain of 2.18. Complex changes have taken place in the cementite lamellae during drawing, which are characterized by lamellar refinement, bending and fracture in morphology, and polycrystalline, amorphous and nanocrystalline phenomena in microstructure. When the pearlitic lamellar orientation is nearly parallel to the drawing direction, interlamellar spacing gradually decreases, the lamellar arrangement direction gradually turns to the drawing direction, and the cementite lamellae become amorphous and nanocrystalline. When pearlite lamellae are nearly perpendicular to the drawing direction, cementite lamellae are bent, fractured and crystallized. At low drawing strain, dislocations mainly move in ferrite phase with a single slip, forming dislocation lines. At high strain, dislocations transform into multi-slip motions, generating dislocation tangles and dislocation cells, and some dislocations slip across the α-ferrite/cementite interfaces. Dislocation interacts strongly with cementite, and the lattice distortion in cementite increases, which is the main reason for the complex changes of cementite lamellae during cold drawing.
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Pilot investigation of catalytic oxidative removal of carbon monoxide from alumina industrial flue gas
Xinglong GU Yang LI Changming LI Zijun GONG Huanyuan NING Ruijian TANG Jian YU
The Chinese Journal of Process Engineering 2025, 25 (1): 89-100. DOI:
10.12034/j.issn.1009-606X.224114
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The calcination process of the alumina industry usually produces nearly 10 000 mg/m3 CO in the flue gas during the combustion process due to low temperature or low excess air coefficient. Direct emissions not only causes energy waste but also causes harm to the local atmosphere. To explore the industrial application feasibility for catalytic elimination of CO from flue gas in alumina calcination, the manganese-cerium particulate industrial catalysts were prepared by co-precipitation method, and the pilot application study with flue gas volume of 1000 Nm3/h was carried out in an aluminum company of Shandong Province. The pilot test results showed that under the condition of low sulfur (<10 mg/m3), when the inlet temperature was 170℃, the CO removal rate was 80%~85%, and the removal rate was above 90% when the temperature was above 200℃. The catalyst was used in the pilot test to run continuously for 500 h at the inlet temperature of 190~200℃. It was found that there was no significant decrease in activity as a whole, indicating that the manganese-cerium catalyst had good stability in the purification of CO gas under actual working conditions. After 500 h of pilot-scale catalyst operation, the catalyst samples at different positions of the fixed bed were analyzed, and it was found that the catalyst performance at the flue gas inlet decreased slightly. The characterization results of typical samples such as XRD, TG, BET, SEM-EDS, and H2-TPR showed that the crystal diffraction peak of the catalyst sample at the flue gas inlet was enhanced, the specific surface area was decreased, and the sulfur deposition was increased, indicating that the local heating sintering and sulfur deposition were the main reasons for the partial deactivation of the catalyst.
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Modal visualization of heterogeneous condensation of water vapor on the surface of a single particle
Xiangcheng WU Li LÜ Lijuan QIAN
The Chinese Journal of Process Engineering 2025, 25 (1): 101-110. DOI:
10.12034/j.issn.1009-606X.224142
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Heterogeneous condensation of water vapor on particle surfaces is a highly valuable industrial pretreatment technique for dust removal. Heterogeneous condensation of water vapor on particle surfaces can significantly improve the efficiency of dust removal. To study the dynamic behavior of droplets on the surfaces of particle during the process of heterogeneous condensation, the environmental scanning electron microscope (ESEM) is employed for visual observation of the heterogeneous condensation process of water vapor on particle surfaces. The evolution process of droplet mode is studied, and the contribution of line tension to the Gibbs free energy of the system during the condensation process and the influence of particle size and contact angle on line tension are analyzed. The results indicate that particles first nucleate to form a critical embryo droplet. This embryo droplet continues to grow and rapidly spreads to the equator of the particle. The droplet then remains on the equator, undergoing continuous condensation and growth, gradually transitioning to crossing the equator. With increasing condensation time, the droplet gradually envelops the particle. Once the particle is completely enveloped, the heterogeneous condensation transforms into homogeneous condensation and continuous growth. The entire condensation process can be divided into five modes: nucleation, diffusion, transition, encapsulation, and growth. The line tension of the five modes is analyzed, and it is found that when the droplet is in the upper hemisphere of the particle, the closer it is to the equatorial line, the greater the contribution of the line tension to the Gibbs free energy change of the system, which promotes its movement towards the equatorial line, and when it is in the lower hemisphere, it promotes its encapsulation of the particle. The effects of particle size and contact angle on the line tension are numerically studied, and it is found that the line tension increased with the increase of particle size. The influence of the intrinsic contact angle of the particle on the line tension is small, but the bigger the difference between the particle and the apparent contact angle, the greater the line tension.
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Cover and Contents
The Chinese Journal of Process Engineering 2025, 25 (2): 0-.
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Research progress of Si
3
N
4
/BN composite ceramics
Lei ZHAO Yue SUN Yulong HU Zheyu FANG Xing JIN Songlin RAN
The Chinese Journal of Process Engineering 2025, 25 (2): 111-128. DOI:
10.12034/j.issn.1009-606X.224154
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Si3N4 is an inorganic nonmetallic material with high hardness, high mechanical strength and high thermal stability. It is widely used in cutting tools, biomedicine, electronics, military and automobile fields. However, due to the hard and brittle characteristics of Si3N4 itself, surface defects are formed during processing, which greatly reduces the reliability of Si3N4 ceramics. A large number of studies show that the composite ceramics prepared with Si3N4 as matrix can effectively make up for the shortcomings of single Si3N4 ceramics. Among them, the composite ceramics prepared by adding BN as the second phase are particularly attractive in advanced engineering applications. BN ceramics exhibit good electrical insulation, oxidation resistance, and corrosion resistance. It has a good application prospect as a heat conductive and insulating material. In addition, the densification process and grain growth of composite ceramics are affected by sintering process, thus changing the properties of composite ceramics. Therefore, the excellent properties of the two materials are taken into account by adding BN to the Si3N4 ceramic matrix, the mechanical properties and dielectric properties of Si3N4-based composite ceramics are improved. In addition to thermal conductivity, Si3N4/BN composite ceramics also have other properties such as burning resistance, thermal shock resistance and microwave absorption. The mechanism research and structural design of sintering technology of Si3N4/BN composite ceramics need to match the current application requirements of ceramic materials, and the further improvement of its properties is still the focus of current research. In this review, the sintering process of Si3N4/BN composite ceramics is introduced, and the research progress of properties of Si3N4/BN composite ceramics in recent years is summarized. Finally, this study outlines the current challenges and areas for further research in Si3N4/BN composite ceramics development.
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Developments and challenges in the evaluation of biological carbon sequestration benefits
Mengdie WANG Xue XIA Dan WANG Zhao QIN Zhiyao PENG
The Chinese Journal of Process Engineering 2025, 25 (2): 129-141. DOI:
10.12034/j.issn.1009-606X.224200
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With the concentration of carbon dioxide (CO2) in the air rising, the threat of global warming is getting worse. Due to its mild conditions and reaction specificity, the biological carbon sequestration technology shows excellent potential for industrial applications under carbon neutral constraints. However, to be genuinely sustainable, industrial applications must implement low-carbon-footprint technology. Current methods for biological carbon sequestration assessment are few and heterogeneous, with the lack of a harmonized scientific assessment framework. In order to promote the development on the biological carbon sequestration assessment, this article reviews the application of genome-scale metabolic network model (GSM) and life cycle assessment (LCA) in biological carbon sequestration assessment, with a focus on analyzing the bottleneck issues of these two methods in biological carbon sequestration assessment. In addition, this review also provides a systematic outlook on the future development direction of the biological carbon sequestration assessment, elaborates on the significant advantages of machine learning applications, points out the scientificity of evaluation indicators based on atomic economy (AE), standardizes the basic framework for data acquisition, and analyzes important breakthroughs in constructing a multi-level evaluation framework.
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Data driven modeling of energy consumption and product quality in ethylene glycol distillation process
Kangkang FENG Xin GENG Qinghui LOU Yu WANG Huajun HU Xiangjian SHI Cuimei BO
The Chinese Journal of Process Engineering 2025, 25 (2): 142-149. DOI:
10.12034/j.issn.1009-606X.224158
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With the rapid development of polyester industry, the increasing demand of ethylene glycol (EG) is in conflict with the shortage of supply in China. Large project of EG production from coal has been receiving more and more attention. In the production of coal-to-ethylene glycol, the optimization of distillation operations represents a vital means to achieve energy saving and consumption reduction, as well as quality enhancement and efficiency improvement. The foundation of optimization lies in the establishment of precise models for the process. However, due to the complex reactions, strong system coupling, and non-linearity inherent in the distillation process, it is difficult to accurately construct models using traditional mechanistic methods. Therefore, this study uses the distillation process of coal-to-ethylene glycol as the research subject, employing a refined least squares support vector machine (LSSVM) algorithm to accurately construct energy consumption and product quality models for the ethylene glycol distillation process. In this process, the actual industrial data from the coal-to-ethylene glycol distillation process was used as the benchmark, the mutual information method was employed to extract the main feature parameters, and variable screening and data pre-processing were conducted. Subsequently, by introducing local target sets and using the UMDA algorithm for iterative optimization, the optimal hyperparameters were derived. After determining the optimal hyperparameters, the improved LSSVM algorithm was used to model the data samples and further compared this model with other purity and energy consumption models established by different algorithms. This comparison confirmed the high efficiency and accuracy of the improved LSSVM algorithm based on UMDA proposed in this work. In summary, compared with traditional support vector machine methods, the LOS-LSSVM model based on the UMDA optimisation process has a clear advantage in data fitting, accurately reflecting the actual situation of the distillation process and effectively improving the operational efficiency of ethylene glycol production.
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Research on influence of oxygen lance area position on flow characteristics of large copper smelting oxygen bottom blowing furnace
Baocheng JIANG Tao XIAO Songsong WANG Xueyi GUO Qinmeng WANG
The Chinese Journal of Process Engineering 2025, 25 (2): 150-158. DOI:
10.12034/j.issn.1009-606X.224173
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With the increasing demand for clean smelting of complex copper containing resources in China, oxygen bottom blowing copper smelting technology is playing an important role, and higher requirements are being put forward for its core equipment's (bottom blowing furnace) smelting capacity. Compared with other bottom blown furnaces, large oxygen bottom blown furnaces have larger specifications and more complex structures, and a high degree of matching between structure and function will be a very important issue. The position of the oxygen lance area is an important factor affecting the fluid flow and mass transfer inside a large oxygen bottom blowing furnace, thereby having a significant impact on the smelting effect. This work takes a large-scale copper smelting oxygen bottom blowing furnace of a certain enterprise as the research prototype, and uses numerical simulation methods to study the influence of the position of the oxygen lance on the flow characteristics of the large-scale oxygen bottom blowing furnace. The main focus is to investigate the influence of the position of the oxygen lance on the functional area and flow field inside the furnace. The results indicate that adjusting the position of the oxygen lance area can alter the distribution pattern of the functional areas inside the furnace. The "one end reaction and one end settlement" mode results in an asymmetric distribution of functional areas within the furnace. The effective extension of the settlement zone is conducive to the full separation of slag and matte. Offsetting the oxygen gun area towards the copper discharge port by 2300 mm form a "reaction at one end and settling at the other" mode. The settling area in front of the slag port is extended by 53.74%, and copper matte and copper slag achieve a more comprehensive and reasonable transition, full separation, and can be used as a directional control measure to optimize production.
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Reaction and gas-solid flow characteristics of calcium carbide synthesis in a fluidized bed
Xu WANG Guohui SU Ting LI Zhennan HAN Liangliang FU Guangwen XU
The Chinese Journal of Process Engineering 2025, 25 (2): 159-168. DOI:
10.12034/j.issn.1009-606X.224166
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Calcium carbide (CaC2) synthesis is a typical high-temperature solid-phase reaction. By reducing the particle sizes of raw material, the intra- and interparticle heat and mass transfer can be significantly improved, thus realizing calcium carbide synthesis at relatively low temperatures and then driving technological revolution. Based on this, a fluidized bed CaC2 synthesis process was proposed in this study, and the reaction characteristics and hydrodynamics of CaC2 synthesis from small-particle raw materials were investigated in a fixed bed and spouted fluidized bed, respectively. Besides, the reactions on the particle surface and its morphological changes during the reaction were analyzed, and the defluidization mechanism was further explored. The results showed that for raw materials with particle sizes of 147~178 μm, CaC2 synthesis reaction can occur at 1500℃, and the reaction rate significantly increased when the temperature was above 1600℃. At 1600℃, the C2H2 yield and CaO conversion rate can reach up to 101~105 mL/g and 25%~26%, respectively. As the C:Ca molar ratio of raw materials was less than 9.6, the defluidization occured when the fluidized bed was operated at 1500~1600℃, and a large number of coke particles were found to adhere to the surface of CaO particle. The bed defluidization was caused by the particle agglomerates, which were formed through the sintering of CaO particles and bonding between CaO and coke particles. It was found that the former was the dominant factor causing defluidization, and increasing the concentration of coke particles in the bed can avoid this. Therefore, this study verified the feasibility of fluidized bed solid-phase CaC2 synthesis and provided a novel approach and data support for technological revolution in the field of CaC2 production.
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Bubble coalescence model considering bubble shape variations and bubble-induced turbulence
Weibin SHI Shanshan LONG Xiaogang YANG Hui HUANG Nian DUAN
The Chinese Journal of Process Engineering 2025, 25 (2): 169-178. DOI:
10.12034/j.issn.1009-606X.224140
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For mathematical modelling of bubble coalescence, the cross-sectional area of the collision tube and the turbulent kinetic energy carried by the colliding bubbles are two key factors to determine the bubble coalescence rate due to turbulent collision. In most coalescence models, the shape of colliding bubbles is assumed to be spheric and the mean turbulent velocity correlation under shear turbulence (ST) condition is used to calculate the turbulent kinetic energy of the colliding bubbles. However, for the gas-liquid bubbly flow, the shape of bubbles transforms gradually from sphere to ellipsoid and spherical-cap with the increase of the bubble's volume. Furthermore, the influence of bubble-induced turbulence (BIT) has shown to be significant in the gas-liquid bubbly flow, especially along with the increase of the volume fraction of gas bubbles. When the bubble coalescence rate is calculated, the shape of bubbles affects the frequency of collision while the dominated turbulence mechanism affects the probability of a successful coalescence event. Based on the Prince and Blanch coalescence model, the present study proposed a coalescence model that considered the bubble shape variations as well as the joint effect of ST and BIT. Also, the turbulent kinetic energy transfer and the eddy-bubble response in the wake of spherical-capped bubble has been considered for the bubble coalescence due to BIT wake entrainment. Population balance model (PBM) has been used in the computational fluid dynamics (CFD) simulations for bubble columns to validate the proposed model. Comparisons have been made via simulation results of bubble size distributions (BSD) predicted by coalescence models with/without considering bubble shape variations and BIT. It is found that considering the shape of bubbles and the joint effect of shear turbulence and BIT, the proposed coalescence model significantly improves the prediction results of BSD and further affects the predictions of other important fluid dynamic parameters.
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Preparation of calcium carbonate nanoparticles by microbubble-enhanced carbonation
Wenxin TIAN Hao DU Biao LIU Shaona WANG
The Chinese Journal of Process Engineering 2025, 25 (2): 179-189. DOI:
10.12034/j.issn.1009-606X.224147
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CO2 mineralization is a promising method for the resource utilization of low-grade limestone and calcium-containing solid waste. Therein, adopting the acetic acid medium to achieve indirect mineral carbonation process to fixing CO2 is considered as an innovative and environmentally sustainable method owing to the reusability of the acetic acid medium. Nevertheless, the conversion efficiency of carbonation in this technique remains limited, with less than 20% efficiency at pressure of 5 MPa. Even with the addition of an extractant for acetic acid, the conversion efficiency of carbonation is still below 30%, significantly impeding the industrial applicability of this technology. In order to address the low conversion efficiency of carbonation in the acetic acid system, this study developed a new method for the preparation of calcium carbonate nanoparticles by microbubble-enhanced carbonation. The impacts of various factors such as medium calcium concentration, reaction temperature, reaction time, the value of pH, and aperture size of aerator on the efficiency of the carbonation reaction were systematically investigated. The results showed that: (1) Under optimal conditions (reaction time of 1 hour, reaction temperature of 80℃, initial pH of 7.2, initial calcium content of 70.07 g/L, and aperture size of aerator of 0.22 μm), the conversion rate of carbonation can reach 19.17% under atmospheric pressure, equivalent to the conversion rate achieved under 3 MPa. Meanwhile the regeneration cycle of the acetic acid medium can avoid wastewater generation at the source. (2) By integrating tributyl phosphate (TBP) with microbubble technology, the conversion efficiency of carbonation was improved to 57.5%, marking a 13.4 percentage point improvement over the reported pressurized extraction process. (3) At atmospheric pressure, rod-like aragonite nano-calcium carbonate products were synthesized with length of 400~800 nm and width less than 100 nm.
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Research on behavior and mechanism of flotation entrainment of microfine-grained serpentine
Jiajun LIU Guofan ZHANG
The Chinese Journal of Process Engineering 2025, 25 (2): 190-200. DOI:
10.12034/j.issn.1009-606X.224160
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In the flotation system of copper-nickel sulfide ores, fine-grained vein minerals, mainly serpentine, are very susceptible to be entrained into the concentrate with the froth, resulting in negative impacts on the concentrate product and the subsequent smelting process. In order to understand the influencing factors and whether there was any interaction in the process of froth entrainment of fine-grained serpentine and other vein minerals in the flotation system of copper-nickel sulfide ores, a response surface analysis (RSA) test was carried out on the basis of a one-factor test, and the effects of the interaction of the three factors, namely, foam agent dosage, gas volume velocity, and the foam layer thickness, were analyzed to determine the effects of the mechanical entrainment. The results of flotation entrainment showed that the foam agent dosage and pulp concentration affected the mechanical entrainment recovery of serpentine by influencing the water recovery and entrainment degree, while the gas volume velocity, particle size, and thickness of the foam layer only affected the entrainment degree and thus the recovery. The response surface test predictions were basically the same as the actual values, indicating that the predictions of the regression model were more accurate and can be used to analyze and predict the test results. The effects of the three factors investigated on the mechanical entrapment recovery of serpentine were foam agent dosage>foam layer thickness>gas volume velocity. Foaming agent dosage and foam layer thickness had significant influence on the mechanical entrainment of serpentine, which was a significant influence factor. The response surface method generally optimized the flotation conditions for the useful minerals rather than the vein minerals, and the interaction analysis showed that the different factors did not interact with each other on the mechanical entrainment of serpentine.
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Dissolution and separation of alumina from Guangxi high-iron bauxite
Hao WU Shuhua MA Yanjun OU
The Chinese Journal of Process Engineering 2025, 25 (2): 201-209. DOI:
10.12034/j.issn.1009-606X.224050
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Taking the unserviceable Guangxi high-iron composite bauxite as the research object, a new three-step process is developed based on clarifying the occurrence forms of alumina in bauxite, the results indicates that they are gibbsite, boehmite, Al-goethite, hematite, anatase, quartz and so on. Among these, iron oxides includes 72.22wt% exists in the form of Al-goethite and 27.78wt% exists in the form of hematite, and the substitution rate of aluminium for iron in Al-goethite is 24.5 mol/mol; Alumina in bauxite exists in three forms, namely gibbsite, boehmite and Al-goethite, each accounting for 37.48wt%, 3.89wt%, and 42.46wt% of the total alumina. Firstly, extract alumina in the forms of gibbsite and boehmite under conditions of Na2O 100 g/L, reaction temperature 180℃, and reaction time 1 hour, which can be easily and completely dissolved, while Al-goethite mineral is difficult to transform under this mild conditions, as seriously affects the economy of this new process. In order to solve the problem of alumina dissolution in Al-goethite, low-temperature roasting is adopted to transform Al-goethite into hematite and activated alumina in order to solve the problem of aluminium leaching from Al-goethite based on the thermal transformation mechanism from goethite to hematite at a certain temperature. By roasting this iron-rich phase for 0.5 h at a temperature of 450℃, about 57wt% of the alumina in Al-goethite is released outside the hematite lattice, thus aluminium-iron separation and phase transformation are achieved. In the third step, the transformed minerals are dissolved again under the conditions of low alkali concentration (Na2O 100 g/L), reaction temperature of 220℃, and reaction time of 1 h. Under these conditions, the activated alumina outside the hematite lattice is dissolved. The total dissolution rate of alumina in the three-step process reaches 85.92%, and the iron oxide in the mineral is greatly enriched in the tailings after dissolution, and its iron oxide content reaches 83.06wt%, which can be used as raw material for ironmaking.
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Preparation and property of colourless polyimide composite films modified with two-dimensional polyaramid
Zijian LI Renzhao WU Haifeng DONG Fenyun YI Yan WANG Defu CHEN Yufu CAI
The Chinese Journal of Process Engineering 2025, 25 (2): 210-220. DOI:
10.12034/j.issn.1009-606X.224184
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Colourless polyimide (CPI) is widely used as covers, substrates and touch panels for flexible displays, which require high glass transition temperatures (Tg), low coefficients of thermal expansion, excellent optical transparency and good mechanical properties. CPI is mainly obtained by introducing fluorine-containing groups to change the chemical structure of the molecular chain. This method of preparation allows for the production of CPI with high light transmittance, although it concomitantly results in a reduction in thermal and mechanical properties. By modifying two-dimensional inorganic materials, the thermal and mechanical properties of CPI can be effectively improved. However, technical difficulties such as poor compatibility with CPI and the complicated modification process also limit the application of two-dimensional inorganic materials in CPI modification. Therefore, a new method for modifying of CPI by a two-dimensional organic polymer, a two-dimensional polyaramid (2DPA) was proposed in this study, 2DPA/CPI composite films were prepared by the solution phase mixing method and the two-step thermoimide method. The structure and properties of 2DPA were analyzed, and the effects of 2DPA additives on the properties of 2DPA/CPI composite films, such as light transmittance, water absorption, Tg, and tensile strength were investigated. The results showed that without compromising the light transmission, the best effect was achieved when the addition of 2DPA in 2DPA/CPI composite films was 1wt%, and the Tg was increased from 338℃ to 358℃ compared to that of CPI films. The tensile strength reached 71.44 MPa, and elongation at break reached 4.34%, which were increased by 21.37% and 24.36%, respectively; and the water absorption rate was reduced by 39%, from 3.33% to 2.03%. The successful preparation of this CPI composite modified with two-dimensional organic material offers new ideas for the research and application of high-performance CPI-based composite materials, holding significant research value.
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Cover and Contents
The Chinese Journal of Process Engineering 2025, 25 (3): 0-.
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Effect of alloying elements on RE
2
Fe
14
B (RE=Nd, Pr) based nanocomposite permanent magnets
Chuanyou HUO Dianbao ZHANG Xiaoyu BO Erbao QIAN Zhen ZHANG Jinghan NIU Shengnan JIANG Hailing LI
The Chinese Journal of Process Engineering 2025, 25 (3): 221-232. DOI:
10.12034/j.issn.1009-606X.224121
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Nanocomposite magnets have become a promising next-generation permanent magnet material due to their potential high magnetic energy product. The implementation of high magnetic performance depends on precise control of the microstructure, including the grain size and distribution of soft and hard magnetic phases, the content of soft magnetic phases, the orientation of hard magnetic phases, the structure and chemical composition, etc. At present, the microstructure of nanocomposite magnets is mainly controlled by adjusting the alloy composition and preparation process. By adding alloying elements, not only can improve the microstructure of nanocomposite permanent magnets, but also can change the intrinsic magnetic parameters of the main phase in the magnet, which is a common method to improve the magnetic performance of the magnet. In this work, the role of alloying elements in microstructure control of RE2Fe14B (RE=Nd, Pr) based nanocomposite permanent magnet materials is summarized and evaluated. The addition of rare earth elements (La, Ce, Pr, Dy, Tb, etc.) to replace Nd atoms alters the intrinsic magnetic parameters of Nd2Fe14B phase. Elements such as Co, Cr, Ni, and Mn can enter the lattice of α-Fe and RE2Fe14B to replace by the point position of Fe, while changing the intrinsic magnetic parameters of the soft and hard magnetic phases, thereby altering the magnetic properties of the magnet. It has been confirmed that elements such as Nb, Ti, and Zr can enter the main phase Nd2Fe14B, but are more enriched at grain boundaries, playing a role in enhancing domain wall pinning and refining grain size. Elements such as Sn and Ga can improve the high-temperature magnetic performance of magnets and enhance their thermal stability. Adjusting the alloy composition through the addition of alloying elements is an effective way to control the microstructure of nanocomposite magnets, but the content of alloying elements should be controlled within a certain range. Excessive addition will deteriorate the magnetic properties of the magnets.
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Heat transfer characteristics of micro-encapsulated phase change material slurry in metal foam filled microchannels
Yongtong LI Jing SUN Weibo WANG Boyu YANG Yunxi YANG
The Chinese Journal of Process Engineering 2025, 25 (3): 233-240. DOI:
10.12034/j.issn.1009-606X.224227
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Micro-encapsulated phase change material slurry (MEPCMs) is a novel kind of functional thermal fluid, which has great potential in the field of electronic thermal management, thermal storage, etc. To improve the thermal management performance of high-power density electronic devices, a dual-enhanced heat transfer method with the combination of MEPCMs and metal foam was employed to improve the cooling performance of mini-channel heat sink in the present study. Numerical methods were utilized to investigate the heat transfer capability, flow resistance, and overall performance evaluation criteria (PEC) by considering the effects of MEPCMs mass fractions (5wt%, 10wt%, and 20wt%), inlet velocities, and metal foam filling ratios. The results indicated that the maximum temperature of metal foam mini-channel decreased and pressure drop increased with increasing the mass fraction of MEPCMs. At an inlet velocity of 0.06 m/s, increasing the mass fraction from 5wt% to 20wt%, the pressure drop increased by 2.09 times. 5wt% MEPCMs presented the best comprehensive heat transfer performance, and the PEC value was improved by 8.15%~12.18% compared with pure water. The filling ratio of the metal foam also significantly affected the heat transfer performance of the microchannel, and the cooling performance was best when the mini-channel was fully filled with metal foam. For the entire range of flow velocities, using 5wt% MEPCMs as the coolant, average Nuave of mini-channel heat sink fully filled with metal foam was 9.06 times of the empty mini-channel heat sink, and the pressure drop came to 56.91 times. With the comprehensive consideration of heat transfer enhancement and flow resistance, the PEC value could reach up to 2.61. The present findings could provide theoretical guidelines for developing more coefficient and compact liquid-cooled electronic devices.
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Effect of solid phase volume fraction on cavitation characteristics of O-type ball valve
Zhaonian ZHOU Binbin WU Tingfeng HUA Zhaotong WANG Zhijiang JIN Wenqing LI Jinyuan QIAN
The Chinese Journal of Process Engineering 2025, 25 (3): 241-248. DOI:
10.12034/j.issn.1009-606X.224257
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The O-type ball valve serves as an important fluid control equipment in the coal chemical industry. However, during the operation process, cavitation phenomenon is very easy to occur inside the ball valve which will greatly affect production safety. The working medium of the ball valve is a fluid containing solid particles, and the volume fraction of particles will affect the cavitation, but the mechanism of how the fraction of particles affect cavitation is not clear. In order to solve this problem, numerical simulation is used to investigate the effect of solid phase volume fraction on cavitation in ball valve under different ball angles. The degree of cavitation in the ball valve can be illuminated by the pressure, cavitation number, and gas phase volume fraction on the valve ball outlet section. The results show that when the ball angle is 30° and 45°, there is no cavitation in the valve under any solid phase volume fraction. However, when the ball angle is 60°, different solid phase volume fractions have different effects on cavitation. When the solid phase volume fraction increases from 0% to 10%, the cavitation degree in the ball valve is gradually weakened. When the solid phase volume fraction increased from 10% to 20%, cavitation in the valve gradually increased. In addition, it is interesting that when the valve ball angle reaches 75°, cavitation in the ball valve will be promoted by any solid phase volume fraction. A lot of work has been done in this work to reveal the influence mechanism of solid phase volume fraction and ball valve angles on cavitation characteristics of O-type ball valves, and some useful results have been obtained, which has a certain guiding on controlling the working environment and multi-phase flow simulation of O-type ball valves.
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Numerical simulation study of pulse soot removal characteristics of pleated cartridge based on fluid-solid coupling
Yifei LI Fuping QIAN Wenyuan HU Qi MA Jinli LU
The Chinese Journal of Process Engineering 2025, 25 (3): 249-260. DOI:
10.12034/j.issn.1009-606X.224243
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Pulse jet airflow is the main means of cleaning dust in the filter cartridge dust collector. The action of the air jet causes the cartridge filter element to expand and shake, and the dust on the cartridge is peeled off and falls into the ash hopper, thus maintaining the clean and efficient filtration performance of the cartridge. In order to more accurately reflect the impact of the blowing airflow on the filter cartridge, the static structural module (Static Structural) in ANSYS Workbench is employed to perform the fluid-solid coupling of the cartridge pulse soot removal, and the resulting pressure is applied to the cartridge. This allows for the conclusions related to the solid mechanics of the filter cartridge under the pressure of pulse blowing to be drawn. By comparing the simulation results with the same blowing time and different blowing distances, the impact of the blowing airflow on the pleated structure of the cartridge can be determined. Firstly, Fluent simulation is employed to obtain the pressure change within the cartridge. It is observed that although the pressure exhibits slight numerical discrepancies under varying blowing distances, its distribution trend remains consistent: the airflow descends along the length of the filter element and subsequently spreads along the radial direction, the static pressure within the cartridge accumulates from the bottom in an upward trajectory. The lower portion of the cartridge exhibits a relatively elevated static pressure, while the upper section displays a comparatively reduced pressure. The accumulation of pressure within the cartridge is discernible. The static structure module in ANSYS Workbench is employed to couple the pressure derived from the Fluent simulation conducted in the preceding step to the pleated structure of the filter cartridge. This enables the acquisition of the total deformation, elastic strain, and maximum shear stress values of the pleated structure of the filter cartridge and their distribution law through simulation under the same time set. In the experimental range, when the blowing distance is 150 mm, the best values of each parameter of the airflow acting on the pleated structure of the cartridge are obtained: the total deformation is 0.133 27 μm, the elastic strain is 3.018×10-4 μm, and the maximum shear stress is 222.69 Pa.
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CFD simulation of bubble columns with tube bundles: impact of turbulence models
Nan ZHANG Xiaoping GUAN Kangjun WANG Ning YANG
The Chinese Journal of Process Engineering 2025, 25 (3): 261-272. DOI:
10.12034/j.issn.1009-606X.224206
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The accuracy of CFD simulation results for bubble columns depends on closure models, such as interphase force models and turbulence models. Most of the previous reports were for empty column without internals, and currently, there is a lack of studies related to bubble column with internals. This study examined the effects of six commonly used turbulence models (Standard k-ε, RNG k-ε, Realizable k-ε, Standard k-ω, SST k-ω, and RSM) on the hydrodynamics in the pilot-scale bubble columns without internals and with tube bundles. The results showed that the RSM predicted significantly higher for turbulent kinetic energy, turbulent dissipation rate, and turbulent viscosity in the empty column compared to eddy viscosity models (k-ε and k-ω models). However, this difference was considerably reduced in the bubble column with tube bundles, and the tube bundles significantly suppressed the turbulence intensity in the liquid phase. Meanwhile, by comparing the simulated gas holdup and axial liquid velocity values with experimental data, it was found that the eddy viscosity models accurately predicted the gas holdup in the central region of the empty column, while the RSM accurately predicted the gas holdup in all regions except the central region. However, the radial distribution of gas holdup predicted by six turbulence models in the bubble column with tube bundles was almost identical, with accurately predicting the gas holdup only in the 0.5<r/R<0.7 region. The Realizable k-ε model's predictions of axial liquid velocity in both empty column and the bubble columns with tube bundles were in good agreement with experimental data, significantly outperforming other turbulence models. Therefore, it was recommended to use the Realizable k-ε model for future simulations of hydrodynamics in bubble columns.
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Investigation of enhanced boiling heat transfer characteristics of hierarchical gradient porous copper surface
Er SHI Shuangrui YE Youlan WANG Qi PENG Bin ZHAO Changwei JIANG
The Chinese Journal of Process Engineering 2025, 25 (3): 273-282. DOI:
10.12034/j.issn.1009-606X.224233
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To enhance boiling heat transfer for promoting the efficiency of the energy system, the porous surfaces with structural gradients were developed on pure copper substrates by employing the electrochemical deposition method. In this study, honeycomb-like porous structures and hierarchical axial honeycomb gradient porous structures were fabricated using constant current single-step deposition and constant current constant voltage two-step deposition methods, respectively. Saturated pool boiling heat transfer experiments were conducted using HFE-7100 as the working fluid to investigate the influence of the gradient pore size changes on the boiling heat transfer performance of porous surfaces. The results demonstrated that the hierarchical gradient porous surface, which had a total deposition time of 60 seconds and an increased second-step deposition voltage of 3 V, showed the most significant heat transfer enhancement. The wall superheat at the boiling initiation point was 9.5 K, a 43.00% decrease compared to the smooth surface at 16.8 K. Moreover, the critical heat flux and heat transfer coefficient reached 522.02 kW/m2 and 22.76 kW/(m2?K), respectively, exhibiting with enhancements of 193.40% and 261.01% compared to the smooth surface. The hierarchical porous surface had two types of nucleation sites: internal pores and dendritic protrusions. The micropores and the internal micropores of the dendrites exhibited a wide range of pore sizes. This extensive distribution of pore sizes not only increased the density of nucleation sites and effective heat transfer area but also reduced the nucleation energy barrier. The axial pore size gradient accelerated bubble evolution, and the capillary suction force provided by the gradient porous structure and dendrites facilitated the return flow of the working fluid to the nucleation sites both horizontally and vertically, thereby enhancing the boiling heat transfer coefficient and critical heat flux of the hierarchical gradient porous surface.
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Numerical study on influence of pulse amplitude on patterns of gas-liquid-liquid three-phase flow in pulsed extraction column with discs and doughnuts
Ting YU Xiucheng YU Zonghui LU Zhe XIAO Ming QU Hui HE Guoan YE
The Chinese Journal of Process Engineering 2025, 25 (3): 283-292. DOI:
10.12034/j.issn.1009-606X.224194
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The pulsed extraction columns with discs and doughnuts play a critical role in the field of spent fuel reprocessing. The countercurrent contact between liquid-liquid two-phase fluids in the column is facilitated through periodic pulses, which significantly influences the separation and purification processes of chemical elements. Although a considerable amount of research on pulse extraction columns with discs and doughnuts has been conducted through simulation, few studies have utilized the actual industrial structure of these columns as examples. A gas-liquid-liquid three-phase flow model coupled with PBM (Polulation Balance Model) to evaluate discrete phase droplet diameter distribution, reflecting the actual structure of pulsed extraction column with discs and doughnuts, was established using CFD (Computational Fluid Dynamics) simulation technology. And it verified the accuracy of the modeling through multiple calculation cases, aiming to investigate the influence of pulse amplitude on the evolution of flow field inside a pulsed extraction column. The model's accuracy was demonstrated through comparison with public literature, and the impact of pulse amplitude on the micro-flow behavior inside the pulsed extraction column was calculated, analyzed and verified. Under the working condition with a pulse amplitude of 1.2 cm, the amplitude had a relatively small impact on the motion of water and oil phases, and the water phase accumulated on the baffle. Under the working conditions of pulse amplitudes of 7.2 and 14.4 cm, the amplitude had a significant impact on the direction and velocity of the water and oil phases, with the water phase separating from the baffle and dispersing into smaller droplets. Furthermore, it was found that as the pulse amplitude increased, both the turbulence kinetic energy and turbulence energy dissipation rate also increased, reaching a maximum value in the region where the fluid impacted the solid wall. Finally, from the distribution of droplet diameter fraction, it was evident that as the pulse amplitude increased, the proportion of small diameter aqueous droplets was higher, which enhanced the extraction. This study used the Euler-Euler two-phase flow model coupled with the PBM to accurately simulate the gas-liquid-liquid three-phase evolution phenomenon in pulse extraction columns, providing a reference for the design and process optimization of subsequent pulsed baffle extraction columns, which laid the foundation for introducing the mass transfer model and heat transfer model through CFD method to analyze the chemical process inside the column in further study.
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Optimization of phosphorus release from anaerobic fermentation of cow manure and phosphorus recovery through vivianite crystallization
Zhihao CHEN Weihua LI Tingting YANG Yixin LIU
The Chinese Journal of Process Engineering 2025, 25 (3): 293-301. DOI:
10.12034/j.issn.1009-606X.224223
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With the rapid development of the livestock and poultry farming industry in China, the disposal and resource utilization of livestock and poultry waste have attracted widespread attention. To maximize the recovery of phosphorus from this waste, this study focuses on fresh cow manure, which is rich in phosphorus, and proposes a novel pathway for phosphorus recovery. By examining the effects of different manure concentrations, anaerobic fermentation durations, and initial pH values on phosphorus release during the anaerobic fermentation of fresh cow manure, the study found that optimal conditions for phosphorus release were achieved with a manure concentration of 180 g/L, an anaerobic fermentation period of 14 days, and the initial pH of 7, resulting in a phosphorus release of 156.57 mg/L. To recover phosphorus from the supernatant of anaerobically fermented cow manure, Fe2+ salts were added to induce the vivianite crystallization. L9(34) orthogonal experiments were conducted to investigate the effects of reaction temperature, pH, and Fe/P ratio on the phosphorus recovery rate. The results showed that the factors affecting phosphorus recovery efficiency in order of significance, were the initial pH value, reaction temperature, and Fe/P ratio. The optimal for the process were found to be a reaction temperature of 35℃, a pH of 7, and a Fe/P ratio of 1.9. Under these conditions, the highest phosphorus recovery rate of 84.20% was achieved, and the purity of vivianite was 25%. The recovered products were characterized using X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR), and Raman spectroscopy. An improved sequential phosphorus extraction method was employed to determine the abundance of vivianite in the recovered products. The research provides a valuable reference for the synthesis of high-value vivianite, based on the effective extraction of phosphorus from fresh cow manure.
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Influence of alumina on reactivity of biopitch anode for aluminum electrolysis
Kunmo ZHANG Wei WANG
The Chinese Journal of Process Engineering 2025, 25 (3): 302-310. DOI:
10.12034/j.issn.1009-606X.224254
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The carbon anode is prepared by baking a mixture of petroleum coke aggregate and pitch at 180℃ for use in the aluminum industry. Due to its good wettability and environmental friendliness towards carbon anode aggregates, the biopitch is considered as a promising carbon anode binder. The biomass conversion technology, substituting traditional coal tar pitch with biopitch, partially or completely in the aluminum production, has recently received domestic and foreign researchers' attention. However, the biopitch typically has a lower coking value which may have a negative impact on its performance. In this work, alumina additives have been added to the biopitch anode to improve its performance. In order to understand the effect of alumina additives on the performance of biopitch anodes, biopitch anode materials were prepared by hot pressing and sintering in the laboratory with alumina as a catalyst. The CO2 reactivity of the anodes was tested with a thermogravimetric analyzer in laboratory. The influence of additives on the performance of the anodes and the CO2 reactivity as well as the wettability of biopitch on petroleum coke were studied by X-ray diffraction analysis, optical microscopy (OM) and high-resolution transmission electron microscopy (HRTEM). The results indicated that the biopitch exhibited better wettability than coal tar pitch with the same surface tension and viscosity. In addition, a transformation occurred from initially less well-ordered to ordered structure for the biopitch anode with alumina additives during baking, thereby increasing the coking value of the biopitch, reducing the CO2 reactivity of biopitch anodes and improving their antioxidant properties. Accompanied by an enhancement in the graphitization degree and an increase of carbon structural orders, the performance of biopitch anodes has been improved significantly with alumina as additives. The biopitch could be used to replace 100% of the coal tar pitch in a carbon anode recipe. This study has provided a theoretical guidance for the application of biopitch anodes and the reduction of energy consumption in aluminum electrolysis.
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Preparation, characterization and release properties in vitro of altrenogest nanosuspension drug delivery system
Chao LI Dongbo LI Yueli WANG Haiyan ZHAO Junhao ZHANG Hualin FU
The Chinese Journal of Process Engineering 2025, 25 (3): 311-322. DOI:
10.12034/j.issn.1009-606X.224240
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Altrenogest (ALT) is oral progestin with poor solubility (~10 μg/mL) and rapid metabolism in vivo, which severely constraints on clinical effectiveness. Nanosuspension drug delivery systems (NS) can reduce the drug particles to nanometer size and improve the solubility and bioactivity of insoluble drugs. The factors and mechanism of altrenogest nanosuspension (ALT-NS) formation were analyzed and investigated using the anti-solvent precipitation method and its quality was evaluated. The preparation process and prescription composition were analyzed and optimized using single factor experiments and the central composite design-response surface methodology (CCD-RSM), and the experiments of characterization, chemical structure analysis, crystalline shape examination, physical stability and release experiments in vitro were applied to evaluate the quality of ALT-NS. The optimal prescription and process were determined as follows: altrenogest 0.4wt%, sodium dodecyl sulfate (SDS) 25 mg/mL, hypromellose (HPMC) 4 mg/mL, stirring speed of 1000 r/min, and stirring time of 10 minutes. The formulation was a light yellow clarified liquid, and the drug particles were in the form of spherical particles with an average particle size of 104.87±1.10 nm, PDI (particle size distribution index) of 0.19±0.01, and Zeta potential of -37.87±0.81 mV, the drug was transformed from crystalline to amorphous state, and the use of freeze-drying technology to make ALT-NS into freeze-dried powder could further improve its physical stability. The cumulative release of the preparation group in vitro was 98.4% at 72 h,which was about 1.54 times higher than that of the original group, showing high efficiency and smooth drug release. In conclusion, the optimization of the prescription composition and preparation process of ALT-NS using the anti-solvent precipitation method can significantly reduce the physical size and specific surface area of ALT, improve the dissolution and release efficiency of ALT, and the formulation has the efficient and fast drug release characteristics, which is expected to provide a reference for the clinical application of ALT-NS.
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Cover and Contents
The Chinese Journal of Process Engineering 2025, 25 (4): 0-.
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Numerical simulation of self-baked electrodes in a Titanium slag three-phase arc furnace
Quan LIU Xiaoping GUAN Ning YANG Jun XIAO
The Chinese Journal of Process Engineering 2025, 25 (4): 323-331. DOI:
10.12034/j.issn.1009-606X.224185
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During the smelting process, the sintering quality of self-baked electrodes determines whether the arc furnace can operate normally. Taking the Panzhihua Steel Titanium Slag Three-Phase Arc Furnace as a prototype, this paper establishes a multi-physics field model of the coupled electromagnetic field and temperature field, and develops a quick calculation method for electromagnetic field and temperature field to accelerate computation. A comparative analysis of current density, Joule heat, and temperature distributions during the baking process of solid/hollow self-baked electrodes is conducted. The results show that both solid and hollow electrodes exhibit a "low at the center, high at the edge" current density distribution, namely the skin effect, with the skin effect of hollow electrodes weaker than that of solid electrodes, resulting in a more uniform current distribution. Besides, the baking regions of solid and hollow electrodes are located within the contact area of the conductive components, indicating that the self-baked electrodes have enough strength to meet the baking requirements. Meanwhile, the time to reach baking equilibrium for solid and hollow electrodes is about 13.4 hours and 12.8 hours, respectively, with the baking time of hollow electrodes being 4.3% shorter.
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Simulation of shape of liquid bridge and gas-liquid interface energy between two ellipsoidal wet particles
Wenzhe WANG Guihuan YAO
The Chinese Journal of Process Engineering 2025, 25 (4): 332-340. DOI:
10.12034/j.issn.1009-606X.224247
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Wet particulate matter widely exists in nature, production and daily life. Surface Evolver was used to investigate the shape of liquid bridge between two ellipsoidal wet particles placed vertically and parallel to each other during the relative rotation and the effects of contact angle, rotation angle, gravity and other parameters were analyzed. Under several different contact angles, the changes in the relative angle between the two particles from 0° to 90° were observed to analyze the changes in the gas-liquid surface area, solid-liquid contact area, and the shape of the contour line obtained by intersecting the plane passing through the center line of the two particles with the surface of the liquid bridge. The differences in the contour line shape of the liquid bridge under the same relative angle with and without gravity were compared. The results showed that the shape of the liquid bridge was a rotationally symmetric body. This body did not satisfy the arc assumption. The variation of the contact angle changed the shape of the liquid bridge. The changes in rotation angle and gravity caused the profile of the liquid bridge to change. Specifically, it changed from an elliptic curve to a hyperbola. The gravity caused the contact line on the upper and lower particles to shift. The rotation of the particles resulted in the reduction of the solid-liquid interface. The gas-liquid interface area of the liquid bridge was sinusoidally related to the relative angle of the particles. The minimum volume required to maintain the liquid bridge under gravity was investigated by gradually reducing the volume of the liquid bridge, and it was shown to be quadratically related to the contact angle and to increase with the increase in liquid density, with the minimum volume required to maintain the liquid bridge when the contact angle was about 90°.
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Migration behaviors and deformation characteristics of discrete bubbles in a variable diameter circular tube
Feng LI Liang MING Lei XING Minghu JIANG Lixin ZHAO Shuai GUAN
The Chinese Journal of Process Engineering 2025, 25 (4): 341-353. DOI:
10.12034/j.issn.1009-606X.224229
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The morphological evolution and migration dynamics of discrete bubbles in variable diameter pipelines have not been clearly analyzed. The deformation dynamics behavior of discrete bubbles in a variable diameter circular tube is an important theory to guide the transport and separation of gas-liquid two-phase mixture. Therefore, high-speed camera technology, combined with numerical simulation, is used to explore the migration and fragmentation mechanism of discrete bubbles in variable diameter pipes. For the structure of a variable diameter circular pipe, a study on the migration behaviors of discrete bubbles in the variable diameter field is conducted under different Reynolds numbers and bubble sizes. The flow pattern, velocity field and bubble deformation characteristics within the variable diameter circular pipe at various inlet Reynolds numbers are analyzed. The aim is to explore the interaction patterns between the flow field characteristics and discrete bubbles and provide theoretical support for revealing the motion and deformation mechanism of discrete bubbles in variable cross-section field. The results indicate that the surrounding fluid velocity is altered by bubbles. The velocity gradients are increased, and the turbulence kinetic energy in the surrounding flow field is elevated. At the same time, the dramatic change of turbulent kinetic energy in the sudden expansion section leads to the rapid deformation or even fragmentation of discrete bubbles in the variable diameter circular tube field. Additionally, as the inlet Reynolds number increases, the fragmentation position of bubbles in the flow field tends to approach the sudden expansion section. When Re=5.16×103, the shortest bubble fragmentation distance is 16.09 mm. When the Reynolds number is constant, as the bubble radius increases from 2.5 mm to 4.5 mm, the dimensionless maximum deformation of the bubble is increased from 0.26 to 0.67. The numerical simulation results demonstrate good agreement with experimental findings.
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Simulation of flow and mixing characteristics of binary particles in gas-solid fluidized bed (I): axial/radial flow field distribution characteristics
Guifang WANG Shuangzhu KONG Jian LI Xiuying YAO Yiping FAN Chunxi LU
The Chinese Journal of Process Engineering 2025, 25 (4): 354-363. DOI:
10.12034/j.issn.1009-606X.224286
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In the fields of petrochemical and chemical engineering, some new processes involving the reactions of gas and catalysts with distinct functions and physical properties have been proposed. Since considerable physical properties difference in density, size and shape between two types of particles,the hydrodynamic behaviors of the binary mixture in the gas-solid fluidized bed are undoubtedly complex. This work presents a numerical investigation on the mixing and flow characteristics of binary particles (Geldart A particles and Geldart D particles) and gas in the bottom region of the gas-solid fluidized bed-riser coupling reactor. Considering the non-uniform structures in intermediate scale, the Eulerian-Eulerian multi-fluid model as well as the drag force model based on the energy minimization multi-scale (EMMS) are used. The axial distributions of bed density and pressure in the binary particle fluidized bed are investigated. By analyzing the turning points of these two parameters, the location of interface between the dense phase zone and the dilute phase zone is determined. The cross-sectional average solid holdup of Geldart A particles and Geldart D particles in the axial direction is also discussed. By comparing the parameter, the relative cross-sectional average solid holdup rates of the two types of catalysts, it is found that most Geldart D particles accumulate at the bottom of the bed in the axial direction. Furthermore, when the binary particle system is composed of coarse particles with low density and fine particles with high density, the distribution of the bed density in the bottom region of the bed layer is steady. In the radial direction, by analyzing the radial distributions of the local solid holdups of the two-solid phase, it is seen that both the Geldart A particles and the Geldart D particles tend to travel towards wall area. By introducing the new parameter, the local relative solid holdup, it is revealed that the Geldart D particle has a stronger tendency towards the wall compared to Geldart A particles.
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Simulation of flow and mixing characteristics of binary particles in gas-solid fluidized bed (II): mechanical analysis of radial distribution characteristics of flow field
Guifang WANG Shuangzhu KONG Jian LI Xiuying YAO Yiping FAN Chunxi LU
The Chinese Journal of Process Engineering 2025, 25 (4): 364-372. DOI:
10.12034/j.issn.1009-606X.224287
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Due to the distinct differences in size, density or shape of the particles' physical properties, the pattern of the two solid phases is complex. The hydrodynamics of binary mixtures of Geldart A particles and Geldart D particles in gas-solid fluidized bed, particularly the radial flow behaviors, are investigated. By comparing relative solid holdup, it is found that Geldart D particles tend to accumulate near the wall. However, few studies have discussed the occurrence for this phenomenon. The Kutta-Joukowski transverse force is introduced to analyze the distribution characteristics of local density and the local fractions of binary particles in the radial direction from the viewpoint of the forces on particles. Considering the fact that non-uniform structures in intermediate scale, the Eulerian-Eulerian multi-fluid model as well as the drag force model based on the energy minimization multi-scale (EMMS) is used. The Kutta-Joukowski transverse force on particles presents a non-uniform distribution in the radial direction. It is related to the gas-solid velocity-difference vector and the particle velocity radial gradient. Based on the radial profile of the Kutta-Joukowski transverse force, the flow regime is divided into three zones, the Kutta-Joukowski uniform influence zone (zone I), the velocity gradient dominant zone (zone II), and the velocity-difference vector dominant zone (zone III). The results show that the Geldart A particles and Geldart D particles exhibit similar tendencies in zone I to move towards the wall, resulting in a uniform distribution. In zone II and III, both Geldart A particles and Geldart D particles are exerted by the Kutta-Joukowski transverse force towards the wall, leading to a core-annulus phenomenon with low concentration at the center and high concentration near the wall. Compared to Geldart A particles, relatively higher Kutta-Joukowski transverse force on Geldart D particles results in a stronger tendency to move towards the wall region in zone II. In zone III, on the other hand, the tendencies for Geldart A particles and Geldart D particles travelling towards the wall are relatively weak.
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Design and performance study on a novel gravity heat pipe based energy storage unit for new energy consumption
Shu ZHANG Yuanlin CHENG Hu YU Yi ZHANG Jinlin XIE Xingwei LIAO Ren ZHANG Changhui LIU Yanlong GU
The Chinese Journal of Process Engineering 2025, 25 (4): 373-381. DOI:
10.12034/j.issn.1009-606X.224288
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As the global climate change issue has been escalating in severity, promoting the transformation of the energy structure has emerged as an irresistible trend. This involves reducing reliance on fossil fuels and enhancing the capacity for new energy consumption, particularly in the field of building heating, which contributes significantly to overall energy consumption. In this work, a solid-liquid phase change/vapor-liquid phase change coupling-based thermal storage heating device is designed, which is essentially a combination of a new type of gravity heat pipe and the phase change material paraffin wax, supplemented by the internal and external heat dissipation fins of the heat dissipation cylinder of the heat dissipation cylinder, enabling the completion of heating through natural convection. The wall temperature characteristics, start-up characteristics, heat transfer performance, and uniform temperature performance of the designed new gravity heat pipe with square liquid cavity are investigated experimentally. Subsequently, the heat storage and release characteristics of the heating unit are studied, and it is concluded that the new gravity heat pipe has good start-up characteristics, heat transfer characteristics, and uniform temperature performance, and its minimum heat transfer thermal resistance can be as low as 0.018℃/W, and the maximum equivalent thermal conductivity is 239.15 kW/(m?℃). The minimum starting temperature is 56.9℃, and the minimum homogeneous temperature coefficient is 0.009. The heating unit has a better heating capacity, with a maximum heating coefficient of 3.83. The design and research results of this new energy storage unit have important reference value for the comprehensive utilization of mobile heating units and distributed energy.
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