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Table of Content

    22 September 2020, Volume 20 Issue 9
    Contents
    Cover and contents
    Chin. J. Process Eng.. 2020, 20(9):  0. 
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    Reviews
    Application and practice of multi-pollutant cooperative control technology for flue gas in iron and steel industry
    Xindong WANG Changjiang HOU Jinglei TIAN
    Chin. J. Process Eng.. 2020, 20(9):  997-1007.  DOI: 10.12034/j.issn.1009-606X.219317
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    The discharge situation of flue gas pollutant from two key processes of coking and sintering in iron and steel industry and the current environmental protection policies of iron and steel industry are analyzed in this study. Base on the analysis of the emission characteristics of flue gas pollutants from coking and sintering processes, and comparing the characteristics of flue gas of power plant, the technical route which can be improved by combining the flue gas treatment mode of power plant and its own characteristics. The environmental protection status of a large state-owned iron and steel enterprise was analyzed based on the desulfurization and denitrification equipment. The advantages and disadvantages of existing source emission reduction, process control and end-treatment technologies for typical pollutants such as sulfur dioxide, nitric oxides and particulate matter are analyzed. Furthermore, combining with the advantages and disadvantages of these technologies, three technical routes to achieve ultra-low emission of flue gas pollutants are put forward in the coking and sintering processes, that are semi-dry desulfurization combined with selective catalytic reduction denitrification, semi-dry/wet desulfurization combined with ozone oxidation denitrification, integrated desulfurization and denitrification of activated coke. This work emphatically introduced the application effect of these technologies in a large iron and steel enterprise, and based on the whole process coupling technology, the multi-pollutant collaborative removal technology and its application in coking and sintering processes were proposed respectively, that were low nitrogen combustion technology combined with terminal technology of multi-pollutant control technology of active coke and sintering flue gas circulation combined with activated coke multi-pollutant cooperative control technology. In the end, based on the application effect of technical routes in this work, the rationalization suggestions were put forward for selecting ultra-low emission technologies in sintering and coking processes of iron and steel industry in the future.
    Flow & Transfer
    Static pressure distribution in a novel gas-solid separator with coupling centrifugal separation and granular bed filtration
    Yuxue LIU Sihong GAO Yiping FAN Chunxi LU
    Chin. J. Process Eng.. 2020, 20(9):  1008-1015.  DOI: 10.12034/j.issn.1009-606X.219358
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    A gas?solid separator which coupled a cyclone with a granular bed filter was put forward. It combined the mechanisms of the centrifugal separation and the filtration. The experiment was carried out under the conditions of both no-dust inlet and the fixed bed mode. The static pressure in the inlet annular space, the separation space and the dust hopper of the coupled equipment were measured. The experimental results showed that the distribution of the static pressure reflected the features of the flow field inside the equipment. Specifically, the tangential and axial distributions of static pressure assumed asymmetric profiles while they increased from the center towards the wall. A static pressure increasing region and a decreasing region in the separation space were observed, respectively. The influences of the negative pressure in the central area and the vortex on the static pressure were not clearly seen below H=6.41D. Moreover, it was also found that a low-velocity area appeared near the outer wall of the granular bed, which believed to be beneficial to the separation efficiency of the proposed separator. Based on the experimental data, a static pressure distribution model covering the physical parameters, the structural parameters and the operating parameters were given.
    Investigation and optimization on catalyst distribution in the inlet region of FCC external catalyst cooler
    Jiantao LI Xiuying YAO Lu LIU Chunxi LU
    Chin. J. Process Eng.. 2020, 20(9):  1016-1024.  DOI: 10.12034/j.issn.1009-606X.219360
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    An external catalyst cooler is used to remove extra heat to ensure the heat balance in the system of fluid catalytic cracking (FCC). However, the single inlet in the cooler is difficult to make the catalysts distributed uniformly in the inlet region. Moreover, the catalysts streaming deviate from the original flow direction due to effect of valve plate. These influence their long period of stable operation. A pilot scale cold mode experimental device was built to study and optimize the catalysts distribution and deviation of flow direction in the inlet region of the external catalyst cooler. The effect of operation conditions on catalysts distribution and deviation of catalysts flow direction was measured. And two new inlet structures were designed to improve the non-uniform flow and deviation of catalysts flow direction. The experimental results showed that for the original inlet structure used in industry, the non-uniform distribution of the catalysts was first increased and then decreased with increasing the solid mass flux (Gs) in inlet tube. The worst circumferential distribution of catalysts occurred at Gs=230~620 kg/(m2?s) and ug=0.2~0.35 m/s. The deviation of catalysts flow direction was determined by locally asymmetric distribution index. The index increased and then decreased as the solid mass flux increased. The maximum value was presented at Gs=380~720 kg/(m2?s). After installing two new inlet structures, the catalysts mass distribution in the inlet region of the external catalyst cooler got more uniform and the deviation of catalysts flow direction was weakened. The inlet structure 2 had better optimization effect on mass distribution and symmetrical distribution of catalysts. Pressure drop in inlet tube with structure 2 increased by about 0.14 kPa compared to that of the original inlet structure.
    Reaction & Separation
    Recovery of sulfuric acid regenerated from stainless steel pickling waste solution by solvent extraction
    Dong ZHANG Jian ZHANG Guanghao SHANG Hui SU Wensen LIU Yun ZHU Zhaowu ZHU Tao QI
    Chin. J. Process Eng.. 2020, 20(9):  1025-1034.  DOI: 10.12034/j.issn.1009-606X.219328
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    As the output of the stainless steel is increasing year by year, the waste acid produced by pickling the stainless steel is also increasing year by year. The waste sulfuric acid solution discharged by pickling the stainless steel contains a large amount of free acid. According to the acid recycling process developed by our research group, the free acid concentration in the waste acid can increase to obtain the regenerated sulfuric acid while quite effectively recovering these valuable metal ions in the waste acid. In this work, the technology of recovering sulfuric acid from the stainless steel pickling waste solution by the solvent extraction was studied, aiming at the problems of high concentration of regenerated sulfuric acid in the stainless steel pickling waste solution, high consumption of neutralization treatment reagent, large amount of waste residue, and so on. It was found that the organic system of 40% (volume fraction, the same below) tris-2-ethylhexylamine (TEHA)+50% isomeric tridecyl alcohol+10% Exxsol D110 was the optimal composition. The extraction rate of sulfuric acid increased with the increased concentration of TEHA. With the temperature increasing of the extraction, the extraction rate of sulfuric acid decreased, indicating that the extraction reaction was exothermic reaction and the enthalpy (ΔH) of the extraction reaction was calculated as ?7.5708 kJ/mol. McCabe-Thiele diagrams were drawn according to the distribution curves of the extraction and the stripping. Under the condition of 30℃ and A/O=1:2, the extraction rate of sulfuric acid could reach 79.8% by 3 stages (theoretical). Using the deionized water as the stripping agent, the stripping rate of sulfuric acid could reach 85.5% after 3 (theoretical) stages at 30℃ and A/O=1:1. The kinetics of the extraction and stripping was very fast and the phase separation was rapid at the same time, which can perfectly meet the requirements of industrial continuous production.
    Removal optimization of methyl orange and Congo red adsorbed on MIEX resin using response surface methodology
    Yunhan JIA Lei DING Peiyue REN Ling LI Dandan WANG
    Chin. J. Process Eng.. 2020, 20(9):  1035-1044.  DOI: 10.12034/j.issn.1009-606X.219335
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    Four factors including resin dosage, solution pH, methyl orange or Congo red concentration and adsorption time were selected to investigate the effects on the removal of methyl orange or Congo red adsorbed on MIEX resin using Box-Behnken response surface methods. According to the experimental results, the quadratic polynomial regression model was established to predict the removal of methyl orange or Congo red. Variance and significance were used to test the reliability of the regression equation. Based on the regression model, the operation parameters of the removal of methyl orange (Congo red) adsorbed on MIEX resin were optimized and the optimal conditions were obtained. Under the optimal conditions, the removal efficiency of methyl orange and Congo red on MIEX resin were 99.12% and 98.29%, respectively. The interaction between solution pH and resin dosage had a significant effect on the removal efficiency of methyl orange and Congo red. The saturated resin adsorbed methyl orange or Congo red were regenerated using NaCl solution, and the surface morphology of MIEX resin were characterized by field scanning electron microscopy. The results showed that the spent resin can be regenerated well with NaCl solution.
    Study of roasting–dissolving performance of high-sulfur and high-silicon bauxite
    Wenjie REN Huixin JIN Chaoyi CHEN Benjun XU Zhenshan XIE
    Chin. J. Process Eng.. 2020, 20(9):  1045-1052.  DOI: 10.12034/j.issn.1009-606X.219334
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    The suspension roasting of bauxite can not only effectively desulfurize, but it can also improve the dissolution properties of low-grade bauxite. Furthermore, it provides a good solution for the industrial utilization of low-grade bauxite with high sulfur and high silicon. In this study, suspension roasting was used to treat high-sulfur and high-silicon bauxite, and the effects of different roasting temperatures on sulfur content were investigated. The effects of roasting on phase transition and microstructure of bauxite were analyzed via XRD and SEM. At the same time, the effect of different calcination temperatures on the solubility of alumina was also studied via dissolution tests. The results showed that suspension roasting desulfurization was feasible. Indeed, the sulfur in bauxite was removed at 550, 600 and 650℃, and the sulfur content in bauxite was reduced to less than 0.2wt% when the suspension roasting temperature was 600℃ or above. As shown by the XRD spectrum, the kaolinite phase in the bauxite was decomposed to form amorphous metakaolin via roasting, and when the roasting temperature reached 600℃ or above, the kaolinite phase was found to be completely decomposed. Furthermore, SEM images indicate that, when the roasting temperature was 600℃, the dense structure of the ore particles was seriously damaged, resulting in grain refinement. On the other hand, local sintering occurred when the temperature reached 650℃. In addition, the diaspore crystal was destroyed by roasting, and the diaspore was activated. In particular, the crystal destruction was found to be most extensive under 600℃ roasting conditions. Thus, the effect of alumina dissolution under the same dissolution conditions was more pronounced than that of row ores and roasting ores at other temperatures. The optimum dissolution conditions were found to be: dissolution temperature of 270℃, caustic concentration of 245 g/L, lime addition of 14wt%, and dissolution rate of 96% or above, which met the requirements of industrial utilization.
    Leaching copper from pyrite tailings in sulfuric acid medium
    Jinsong YE Tianhu CHEN Mengjuan TANG Yuhui LI Xinlai WEI Jie JIN Ke WU
    Chin. J. Process Eng.. 2020, 20(9):  1053-1062.  DOI: 10.12034/j.issn.1009-606X.220081
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    In order to reutilize these industrial wastes of pyrite tailings, the effects of the six single factors of sulfuric acid concentration, leaching time, ore particle size, ore dosage, leaching temperature and agitation speed on leaching copper in the pyrite tailings and the subsequent L18(37) orthogonal optimization experiments had comprehensively been investigated. Furthermore, the mechanism inhibiting further acid leaching reaction had been revealed by the scanning electron microscopy (SEM) and energy dispersive spectroscopy (EDS). The research result showed that the optimal condition of leaching copper was sulfuric acid mass fraction of 30%, leaching time of 6 h, ore particle size of 150 ?m, ore dosage of 5 g, leaching temperature of 108℃, and agitation speed of 440 r/min. Under the condition, the Cu leaching rate can reach 50.68%. The priority of influencing factors of sulfuric acid mass fraction>leaching temperature>ore dosage>leaching time>ore particle size>agitation speed was obtained via the range analysis of the orthogonal test, and moreover the six factors were extremely significant via the variance test. Finally, the SEM and EDS had revealed that the surfaces of the leached residues had tightly been encapsulated by micron-sized particulate SiO2, so that it passivated the further leaching reaction progress and limited the constant increase of the leaching rate at the late stage of acid leaching. Therefore, it was very necessary to loosen the SiO2 coating layer and release its passivation at the later stage of leaching reaction for the sake of further improving the leaching copper in the silicon-rich pyrite tailings.
    Process & Technology
    Studies on association equilibrium of Mg2+ and SO42+ by confocal Raman spectroscopy
    Bo YAN Huan ZHOU Shuixiu LI
    Chin. J. Process Eng.. 2020, 20(9):  1063-1073.  DOI: 10.12034/j.issn.1009-606X.219349
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    Magnesium Sulfate solution is an important electrolyte solution which is widely used in many fields. The characteristics and the association equilibrium of Mg2+ and SO42- have been the focus of attention, which has important application values. In this paper, the characteristic of ion association structure of Mg2+ and SO42- in different concentration MgSO4 solutions at different temperature were studied by Raman Spectroscopy combined with Gauss-lorentz peak fitting program. Furthermore, the ion association equilibrium constant KR of MgSO4 solutions were calculated. Furthermore, the apparent thermodynamic parameters of the associated reaction of Mg2+ and SO42? and the product of the contact ion pair CIP′under standard state were inferred. The spectra experiments results showed that the peak area and peak intensity of the ν1-SO42? characteristic peaks in MgSO4 solution were linearly associated with the concentration of SO42?. The free SO42- ion was the main structure of ν1-SO42? characteristic peaks. During the process of the temperature increasing for high concentration of 1.5mol/L and 2.0mol/L MgSO4 solution, the peak area and peak intensity of the ν1-SO42? characteristic peaks decreased, red shift phenomenon occurred in the peak position, and the symmetry of the peak changed. Accordingly, the content of free SO42- ions decreased, the chance of monodentate contact ion pairs (CIPs) increased, but the content of bidentate CIPs and SO42- groups structure changed irregularly. Likewise, the ion association equilibrium constant KR of MgSO4 solution increased which showed that the ion association equilibrium moved to the right with the temperature increasing for 1.5mol/L and 2.0mol/L MgSO4 solution, thus more CIPs generated. In dilute MgSO4 solutions, there were almost no bidentate CIPs and SO42- groups structure detected, the ion association structure of ν1-SO42? characteristic peaks and KR value changed irregularly. At the same temperature, the KR value decreased exponentially with the increasing of the concentration of MgSO4 solution.
    Effect of P2O5 on lime dissolution process in steelmaking slag
    Yanbo CAO Yunjin XIA Jie LI Dingdong FAN
    Chin. J. Process Eng.. 2020, 20(9):  1074-1081.  DOI: 10.12034/j.issn.1009-606X.219324
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    The dissolution behavior of lime in two groups of slag systems under static conditions was studied by introducing lime blocks with an average size of φ15 mm?10 mm into CaO?SiO2?FeO and CaO?SiO2?FeO?P2O5 slag at 1400℃. The results showed that four areas were formed along reaction interface around in two slag, namely base slag layer, C2S permeable layer, calcium ferrite permeable layer and lime layer. C2S permeable layer and calcium ferrite permeable layer were formed by the interpenetration of Ca2+ in lime and Fe2+ in liquid slag. The presence of a dense solid phase layer in the permeable layer affected the dissolution of lime. The calcium ferrite layer in the permeable layer was gradually replaced by C2S layer. The thickness of C2S layer increased and reached maximum. Finally C2S layer was dissolved in liquid slag. The dissolution rate of lime in the two groups of slag was similar in reaction time of 5~60 s, and the dissolution rate of lime in phosphorus-containing slag was significantly accelerated in reaction time of 60~80 s. When P2O5 was added to the slag, phosphorus was dissolved in C2S to form a C2S?C3P solid solution layer. The formation of this layer will displace FeO into the slag, improve the permeability of the slag, and accelerate the dissolution of lime.
    Continuous flow synthesis of methyl acetoacetate in microchannel reactor
    Jianwu LIU Han JIANG Shenghu YAN Yue ZHANG Jiefa SHEN Daixiang CHEN
    Chin. J. Process Eng.. 2020, 20(9):  1082-1088.  DOI: 10.12034/j.issn.1009-606X.219308
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    Synthesis using traditional batch reaction system has many problems. First of all, it is difficult to control temperature. Secondly, the production capacity is low, and lastly, the reaction time is more. In this work, using diketene and methanol as starting materials, a new method for synthesizing methyl acetoacetate in a microchannel reactor with variable diameter pulse structure, was explored. The method mainly studied the catalyst type, material ratio, residence time, reaction temperature, and catalyst dosage. The best combination of conditions included sodium methoxide as the catalyst, n(diketene):n(methanol):n(sodium methoxide)=1:1.1:0.02, reaction temperature of 90℃, and residence time of 90 s. Under these conditions, the conversion rate of diketene was 100% and the selectivity of methyl acetoacetate was 96.8%. Compared with the traditional batch process, the operating mode of the reaction was updated and the reaction was carried out in an entirely continuous manner. This could achieve continuous automatic control of the process, thus preventing process fluctuation, unstable product quality and safety concerns caused by intermittent manual operation. The challenge was to provide reliable guaranty of heat transfer, mass transfer, environmental protection, and safety. Through process enhancement, precise temperature control, and reduction of liquid holding capacity, the production of by-products was greatly reduced and the production capacity was significantly improved. The microchannel reactor showed strong mass transfer and heat transfer conditions, which strengthened the reaction conditions and completed the reaction in a short time. The safety parameters of the reactor were good, the liquid holding capacity in the reaction zone was small, no unstable intermediates remained, the system was closed, the amplification effect was weak, side reactions were lesser, yield was higher, reaction could be precisely controlled, product quantity increased, there was energy saving and emission reduction, and also quick response to unexpected situations.
    Improving the accumulation of semi-autogenous grinding mill hard stones of a copper?nickel ore in Xinjiang
    Qian ZHANG Qingfei XIAO Xudong WANG Sen YANG Shuai MA
    Chin. J. Process Eng.. 2020, 20(9):  1089-1096.  DOI: 10.12034/j.issn.1009-606X.219347
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    Aiming at the problem that the semi-autogenous grinding mill of a copper?nickel ore in Xinjiang is seriously accumulated and the fineness of the grinding products is not up to standard, based on the determination of the mechanical properties of the ore, the fineness comparison of the semi-autogenous grinding mill grinding products was studied. In the method, the steel ball medium ratio was taken as a single variable, and the comparison test of the grinding index was carried out. The discrete element method was used to verify the laboratory test conclusions. In the end, the optimal medium ratio scheme of the semi-autogenous grinding mill was determined as follows: ?150:?120=1:2. The results showed that the average specific weight was 3.36 g/cm3, the average hardness coefficient was 7.93, the average static elastic modulus was 3.11×104 MPa, the average poisson′s ratio was 0.26, the ore was moderately hard as well as the ore with brittleness and toughness existed. Under the same grinding cycle conditions, the yield of 25~80 mm fraction of the hard stone grade gradually reduced in the recommended scheme of the semi-autogenous grinding mill. The plant scheme was reversed. After the three grinding cycles, the yield of 25~80 mm fraction of hard stone in recommended scheme was 4.19 percentage points lower than that in the plant scheme. The yield of three size fraction of +100, ?2.5 and ?0.074 mm were 0.25, 13.79 and 4.80 percentage points higher than that in the plant scheme respectively. Compared with the larger scheme, the recommended scheme showed better grinding ability as well. Under the same number of grinding cycles, the yield of 25~80 mm fraction of recommended scheme reduced by 3.36 percentage points, and the fineness of ?0.074 mm increased by 2.24 percentage points. The sum of the normal energy utilization of the recommended 25~80 mm fraction was 56.19%, which was 1.82 and 2.30 percentage points higher than the plant scheme and the larger scheme respectively. The recommended scheme showed better hard stone crushing ability. The results of the simulation tests were consistent with the laboratory test results. Based on the comparison of the test results, the recommended scheme had obvious advantages. Ensuring the fineness of the grinding products was in a good level, the accumulation of hard stones was fully solved, which provided a method to learn for a similar problem for related factories and mines.
    Biochemical Engineering
    Isolation and identification of XXG a strain of Paenibacillus with algae-lysing ability and study on algae-lysing characteristics
    Jingjing XUE Meijuan WANG Linqiang MAO Mingfei ZHAN Jun NING Wenyi ZHANG
    Chin. J. Process Eng.. 2020, 20(9):  1097-1105.  DOI: 10.12034/j.issn.1009-606X.219303
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    A strain of bacteria XXG was isolated from rice fields irrigated from Taihu Lake. The bacterial genus was determined by analyzing its morphological characteristics, physiology biochemistry experiment and 16SrDNA sequence. Single factor test was conducted on the addition ratio of medium, the volume ratio of bacteria to algae, the density of bacteria and density of algae to study the effect of each factor on the effect of lysing algae. Box-Behnken Design (BBD) was used to design three major factors, namely, temperature (X1), pH (X2) and shaker speed (X3), to optimize the environmental factors that affect the lysing rate of algae. The method of lysing algae was initially examined by comparing the effect of bacterial weight suspension and sterile fermentation liquid on algal liquid. The experimental results showed that the similarity degree between XXG and Paenibacillus sp. KU573975 was 99.27%, and was initially identified as Paenibacillus. When the optimum volume ratio of bacterial to algal was 5.6%, the lysing rate of XXG bacteria to Microcystis aeruginosa solution at the early logarithmic growth stage reached at 77.1% after 6 d. Three important environmental factors that affected the efficiency of XXG algal lysing had a cross effect. The quadratic regression model of lysing rate of algae with the temperature, pH and shaker speed was established with P<0.0001 and R2 was 0.9727. Under the optimal algae-lysing characteristics, the lysing rate of algae was the highest when the temperature was 30℃, the pH was 7.5, and the shaking speed was 150 r/min, and the lysing rate of algae was up to 92.02%. Aseptic fermentation liquid without algal bacterial still had algae-lysing effect. It was speculated that the main algae-lysing processing of XXG bacteria was indirect effect. The reduction in algae-lysing effect produced by aseptic fermentation liquid compared with bacterial fermentation liquid may be achieved by the bacteria in bacterial fermentation liquid continuing to secrete some algae-lysing active substances.
    Preparation and evaluation of polyvinyl alcohol/bovine type I collagen scaffolds
    Di MENG Xiongxin LEI Yang LI Dawei HUANG Guifeng ZHANG
    Chin. J. Process Eng.. 2020, 20(9):  1106-1113.  DOI: 10.12034/j.issn.1009-606X.219312
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    Collagen is an excellent biomedical material with biocompatibility and biodegradability. However, the poor stability and low mechanical strength of collagen limit its application. Polyvinyl alcohol has good physical and chemical properties which can form a good bio-scaffold material by chemically coupling with collagen. Bioartificial liver (BAL) support has been researched and widely used in providing a bridge to patients waiting for a liver transplant or promoting liver regeneration, which can prevent complications caused by liver failure and improve survival rate. The scaffolds of BAL are important for the reproduction and biological function of liver cells. Polyvinyl alcohol (PVA) and collagen (COL) composite scaffolds was prepared in this work. PVA was modified by the amino silane and collagen crosslinked by glutaraldehyde. Then the heterogeneous mixture was treated by lysine and freeze-dried to obtain the PVA/COL composite scaffolds. The physical and chemical properties of the scaffolds were analyzed by scanning electron microscopy (SEM), X-ray photoelectron spectroscopy (XPS) and Fourier transform infrared spectroscopy (FT-IR). The biological properties of the scaffolds were evaluated by laser confocal, scanning electron microscopy (SEM) and CCK-8 experiments. FT-IR and XPS experiments demonstrated that collagen was successfully coupled to the PVA sponge and maintained a good triple helix structure. The results showed that the pore diameter of PVA modified by COL had uniform pore distribution with porosity of 21.33% and pore diameter of 168.68 μm. The contact angle of the scaffold material was 20.03°. The biological evaluation of scaffold materials showed that C3A cells adhered well on the PVA/COL scaffold and the proliferation test showed that the cells grew well on the composites. The proliferation of cells on the composite scaffolds was significantly different from the control group (P?0.01). The scaffolds prepared by the combination of PVA and COL had a promising application with the good physical and chemical properties.
    Environment & Energy
    Synthesis of polyacrylic-acid-modified Fe3O4@C core–shell microspheres for lithium-ion battery anodes and their electrochemical properties
    Lin ZHU Fangyu WANG Jie LI Yangzhou MA Guangsheng SONG Ailin XIA
    Chin. J. Process Eng.. 2020, 20(9):  1114-1120.  DOI: 10.12034/j.issn.1009-606X.219340
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    Owing to its long cycle life, high energy density, low self-discharge performance, good thermal stability, and insignificant memory effect, lithium-ion battery (LIB) has attracted research attention as one of the most promising energy storage devices. In this study, as LIB anode materials, polyacrylic acid (PAA)-modified Fe3O4@C core–shell microspheres were synthesized by a hydrothermal method using glucose as the carbon source, and their electrochemical properties were investigated. As-obtained samples were analyzed by X-ray diffraction (XRD), scanning electron microscopy, thermal gravimetric differential thermal analysis (TGA–DTA), and Fourier transform infrared spectroscopy (FT-IR). The electrochemical performance was investigated, including cyclic voltammetry performance, cycle life, rate performance, charge-discharge cycles, and impedance curve fitting. The PAA-modified Fe3O4@C core–shell structure was successfully prepared. Uniform microspheres with a particle size of ~310 nm were obtained, in addition to a uniformly coated carbon layer with a thickness of ~30 nm. In addition, the Fe3O4@C core–shell structure effectively relieved the volume expansion during constant current charge and discharge cycles and prevented the rapid collapse of the crystal structure. A large number of carboxyl groups in PAA exhibited a surface modification effect on Fe3O4, effectively preventing particle agglomeration and ensuring good dispersibility. The effective carbon coating can improve the electrochemical performance of Fe3O4 as the anode material of LIB. The enhanced ionic and electronic conductivities were beneficial for its specific capacity, coulombic efficiency, and cycle stability. Moreover, the Fe3O4@C core–shell microspheres maintained a specific capacity of 655 mAh/g after a constant current charge and discharge cycle of 370 cycles at a current density of 100 mA/g; hence, Fe3O4@C core–shell microspheres can be considered as good candidates for application as LIB anode materials.