Loading...
Welcome to visit The Chinese Journal of Process Engineering, Today is

Table of Content

    22 April 2021, Volume 21 Issue 4
    Contents
    Cover and Contents
    Chin. J. Process Eng.. 2021, 21(4):  0. 
    Asbtract ( )   PDF (808KB) ( )  
    Related Articles | Metrics
    Reviews
    Application progress of typical process intensification technologies applied for nanomaterials preparation
    Chunyu SONG Puxuan NIE Shoutao MA Guoyu REN
    Chin. J. Process Eng.. 2021, 21(4):  373-382.  DOI: 10.12034/j.issn.1009-606X.220108
    Asbtract ( )   PDF (644KB) ( )  
    Related Articles | Metrics
    Nanomaterials, regarded as the new materials of the 21st century, have been applied in the fields of chemical, electronics, defense, ceramics, etc. Traditional nanomaterial preparation methods have difficulties in particle size control, poor repeatability, and scale-up effect of industrial application. Process intensification (PI) technology is one of the highly promising directions in the chemical engineering field. PI technology is aiming for the goal of reducing operation unit, decreasing equipment volume, increasing production capacity, and improving energy utilization efficiency by adopting new equipments and new processes for the chemical industry, because the new process may lead the chemical industry to be more safe, friendly and efficient. Therefore, PI technology was superior to conventional methods. Through adjusting preparation time and energy efficiency, nanomaterials with particular morphology and properties could be obtained in some instances. In the past two decades, process intensification has been widely used for nanomaterial preparation, obtaining economic and social benefits, which has attracted more and more attention from scientific researchers. In this work, combining some typical examples, the recent developments in using PI technology for the preparation of nanomaterials as well as their related applications were reviewed, the characterizations and advantages of macrostructure chemical process were summarized, applications of process intensification technologies, such as hypergravity, micro chemical engineering, plasma, ultrasound, microwave, and ionic liquid, for the preparation of nanomaterials were reviewed and prospects were also discussed.
    Analysis of development trend in field of ionic liquids based on global patent information
    Zheng ZHENG Hongyan HE
    The Chinese Journal of Process Engineering. 2021, 21(4):  383-393.  DOI: 10.12034/j.issn.1009-606X.221009
    Asbtract ( )   PDF (701KB) ( )  
    References | Related Articles | Metrics
    Nowadays, countries all over the world pay more and more attention to environmental protection and green development. Ionic liquids have broad application prospects in many fields such as energy, materials and environment, due to its excellent physical and chemical properties and electrochemical properties. Based on global patent information, a comparative analysis was made on the global patent application trends, application regions, important patentees and key technologies of three popular applications in the field of ionic liquids, including CO2 capture and utilization, electrochemical energy storage, biomass conversion and utilization. It is found that ionic liquid technology has a wide classification layout and especially the related patents of catalytic separation are abundant. There are a large number of patent applications in the field of ionic liquids in China, but the patentees are mainly universities or scientific research institutions, and the patent transformation, application and protection are insufficient. Therefore, it is suggested that China strengthen the cooperation between research institutions and new energy/environmental protection technology companies in the field of ionic liquids, and carry out in-depth applications in power batteries, carbon capture, bio-based materials, wastewater treatment, air purification and other fields.
    Flow & Transfer
    Effect of aerator arrangement on aeration performance in oxidation ditch
    Xiaofei XU Wenze WEI Xin DONG Fengxia LIU Wei WEI Zhijun LIU
    Chin. J. Process Eng.. 2021, 21(4):  394-400.  DOI: 10.12034/j.issn.1009-606X.220123
    Asbtract ( )   PDF (1115KB) ( )  
    Related Articles | Metrics
    The experimental study of oxygen transfer performance of clean water and activated sludge mixed liquor in a pilot-scale oxidation ditch of microporous aeration had been carried out. The effect of different aerator arrangement modes (cross, abreast and centralized) on oxygen transfer efficiency were investigated in the experiment. Moreover, the standard oxygen transfer efficiency (SOTE) and oxygen transfer efficiency (OTE) were used as parameters of oxygen transfer performance in the clean water and activated sludge mixed liquor, respectively. The results showed that the oxygen transfer efficiency was affected by the aerator arrangement mode significantly, and the oxygen transfer performances between clean water and activated sludge mixed liquor were different. The oxygen transfer efficiency under the cross aerator arrangement mode was the highest, the abreast aerator arrangement mode was the second, and the centralized aerator arrangement mode was the lowest. In the activated sludge mixed liquor, when the DO concentration was between 1.3 mg/L and 1.7 mg/L, the oxygen consumption of nitrogen removal in different aerator arrangement modes was almost the same. However, the aerator arrangement mode had greater impact on oxygen consumption of COD removal. Compared to the SOTE in the clean water, the OTE in the activated sludge mixed liquor was lower, and the OTE was about 85% of SOTE. Moreover, the OTE was less affected by the aerator arrangement mode than SOTE. To evaluate the aeration performance in the activated sludge mixed liquor, the ratio Z (OTE/SOTE) of oxygen transfer efficiency between the activated sludge mixed liquor and clean water was introduced. Contrary to the regularity of oxygen transfer efficiency under different aerator arrangement modes, the OTE/SOTE was the largest in the centralized aerator arrangement mode and the smallest in the cross aerator arrangement modes. The OTE and SOTE was close under the aerator arrangement mode of low oxygen transfer efficiency.
    Effect of arrangement of multiple groups of twisted slices on product yield in ethylene cracking furnace
    Xingchen HE Juan WANG Jia ZHANG Jiayi WAN Jiangyun WANG Yu MAO
    Chin. J. Process Eng.. 2021, 21(4):  401-409.  DOI: 10.12034/j.issn.1009-606X.220082
    Asbtract ( )   PDF (1359KB) ( )  
    Related Articles | Metrics
    The production of ethylene by cracking furnace is the most commonly used method in industrial and furnace tube is the main place where cracking reactions occur. The internal components of the twisted slices are added to furnace tube and the purpose is to improve the coupling between the flow field and the temperature gradient field, so as to enhance the heat exchange of the fluid and to promote the increase of products in the cracking reaction. U-shaped tube of ultra-selective cracking furnace was selected as the research object, based on naphtha cracking raw material. The furnace tubes were built into different multiple groups of twisted slices for numerical simulation to obtain the temperature distribution and the mass fraction distribution of ethylene and other products. Simulation results showed that the twisted slices can effectively reduce the temperature gradient between the tube wall and the core fluid, and the heat exchange effect of the furnace tube with 3 groups of twisted slices placed in the outlet section was the best. The yield of ethylene and butadiene in the furnace tube increased linearly along the axial distance, while the yield of propylene decreased at the exit stage in the later period of reaction. The L2R3-type tube with two twisted slices placed in the inlet section and three twisted slices placed in the outlet section had higher yield of triene, which was 1.29 times that of the smooth tube.
    Influence of scrap on bath flow characteristics of converter
    Xiaobin ZHOU Shiheng PENG Yong LIU Duogang WANG
    Chin. J. Process Eng.. 2021, 21(4):  410-419.  DOI: 10.12034/j.issn.1009-606X.220131
    Asbtract ( )   PDF (1134KB) ( )  
    Related Articles | Metrics
    The current study focus on the flow characteristics and the effects of scrap on the bath flow with the help of mathematical model which is built based on the physical model of a 250 t converter. The results showed that the mixing time was a decreasing function of the flow rate of bottom blowing when the flow rate was relatively low (<40 L/min). On the contrary, excessive high flow rate of the bottom blowing would not contribute on the decreasing of the mixing time which demonstrated that increasing flow rate was not favorable for decreasing the mixing time if the flow rate was higher than the critical value. With increasing the scrap volume, the plume formed in the bottom blowing moved towards to the bath wall. Meanwhile, the maximum velocity of the plume increased from 0.24 m/s to 0.40 m/s when the bottom flow rate was 50 L/min compared to the flow rate of 15 L/min. The kinetic energy of the bath was increased while the volume ratio of the low-velocity zone was decreased when the scrap volume increased. The volume ratio of the low-velocity zone can be decreased 89.46% when 40 t scrap was added into the bath compared to that of no scrap addition. Specifically, compared to that of 15 L/min when 60 t scrap was added, the transfer indexes decreased 2.98%, 6.27% and 8.68% when the bottom flow rate increased to 25, 40 and 50 L /min, respectively. The effects of the scrap volume on the energy transfer index was also investigated and the results showed that increasing the scrap volume was benefit to increase the energy transfer index for the bath and large volume of the scrap greatly increased the energy transfer index. When the bottom flow rate was 25 L/min, the energy transfer index increased 2.48% and 41.41% when the scrap volume increased to 10 and 60 t, respectively.
    Experimental study on pressure drop characteristics and minimum fluidization velocity of gas-solid micro-fluidized bed
    Yaqi SHI Yanjun LI Yupeng DU Wanzhong REN
    Chin. J. Process Eng.. 2021, 21(4):  420-430.  DOI: 10.12034/j.issn.1009-606X.220332
    Asbtract ( )   PDF (634KB) ( )  
    Related Articles | Metrics
    The fluidization characteristics of Geldart group A and Geldart group B particles were investigated in four gas?solid micro fluidized beds with different inner diameters ranging from 3 to 20 mm, respectively. At the same time, the variation rules of the minimum fluidization velocity affected by some important factors, such as bed geometry, operating conditions and physical-phase properties were studied. The result showed that the bed pressure drop characteristics in the gas?solid micro fluidized bed were closely related to the used particle type, and the flow characteristics of two types of particles were significantly different under various flow states. In the fixed bed stage, compared with Geldart group B particle, the interaction between the A particles and the wall was stronger, leading to greater deviation of the experimental pressure drop value from the calculated value derived from the pressure formula of traditional fluidized beds. While in the fluidized bed stage, the larger particle size and density of Geldart group B particles showed higher bubble coalescence and rupture degree in the fluidized bed, which intensified the collision among different particles and increased the energy loss, as a result the pressure drop of the whole fluidized beds showed a higher experimental value. The minimum fluidization velocity of the gas?solid micro fluidized bed was not only related to the general operating conditions and gas/solid phase properties but also influenced observably by the inside diameter and the height of the static bed. The minimum fluidization velocity increased gradually with the decreased of bed diameter and increased of the static bed height. An empirical correlation to predict the minimum fluidization velocity of the micro fluidized bed was proposed within the scope of the experimental investigation under the condition of some important influencing factors.
    Process & Technology
    Effect of water on microstructure and transport properties of ionic liquids
    Yandong GUO Linlin YOU Xiaochun ZHANG
    Chin. J. Process Eng.. 2021, 21(4):  431-439.  DOI: 10.12034/j.issn.1009-606X.220117
    Asbtract ( )   PDF (979KB) ( )  
    Related Articles | Metrics
    Due to the unique structure and excellent physicochemical properties, ionic liquids have shown a broad application prospect. However, some water inevitably exists in ionic liquids during applications. The presence of waters has a significant impact on the structure and properties of ionic liquids. In this work, the microstructure, interactions and transport properties of [Bmim][B(CN)4], [Bmim][PF6] and [Bmim][Tf2N] with different contents of water were systematically studied by molecular dynamics simulations. By analyzing the number of hydrogen bonds for the system of ionic liquids and water, it was found that the number of hydrogen bonds between anions and water increased significantly with increasing water content, while the number of hydrogen bonds between anions and cation decreased gradually with the increase of water content. The number of hydrogen bonds between anions and water were greater than those between cations and water. The self-diffusion coefficients for the mixture of ionic liquids and water were calculated. It was found that the self-diffusion coefficient of the ionic liquid increased gradually with the increase of the water content. The more hydrophilic the ionic liquids were, the more the diffusion coefficient increased. The radial distribution function and coordination number results showed that the interaction between anions and water was stronger than that between cations and water. However, addition of water to ionic liquids was found to have no impact on the structure between anions and cations. In addition, the results of the spatial distribution function suggested that the distribution of anions and water around H5 and H4 of imidazolium cation ring were competitive, which reduced the interaction between cations and anions. This research results can help to further understand the microscopic mechanism of ionic liquids and water system and promote the application of ionic liquids.
    Reduction of magnesium oxide in calcined dolomite with a mixture of aluminum and ferrosilicon
    Yaoning WANG Hongzhou MA Zhixian WANG Dingding WANG Bixia WANG
    Chin. J. Process Eng.. 2021, 21(4):  440-445.  DOI: 10.12034/j.issn.1009-606X.220138
    Asbtract ( )   PDF (475KB) ( )  
    Related Articles | Metrics
    The Pidgeon process is the main process of magnesium production. The higher reduction temperature of the silicothermic process results in high energy consumption in the magnesium reduction process. Improving the reducing performance of reducing agents was one of the ways to reduce the energy consumption of metallic magnesium production. The theoretical and experimental research on the reduction of MgO in calcined dolomite was studied by the mixture of aluminum and ferrosilicon as reducing agents. The effects of aluminum dosage, reduction time and temperature on the reduction rate of magnesium were discussed. The reduction process of magnesium oxide and the phase transformation of aluminum and ferrosilicon at different temperatures were studied. The results showed that when aluminum was involved in the reduction of magnesium oxide by silicothermic method, the initial reaction temperature of reduction of MgO by silicothermic method was reduced to below 700℃, and the effect of improving the reduction rate of MgO was obvious in the low-temperature stage. The reduction process of magnesium oxide by aluminum included two aspects. On the one hand, it was directly involved in the reduction of magnesium oxide to MgO?Al2O3. With the increase of temperature, MgO?Al2O3 was further reduced by aluminum. On the other hand, aluminum and ferrosilicon from the Al3FeSi2 phase, which promoted the reduction of silicon and reduced the temperature of silicon participating in the reduction of magnesium oxide. In the presence of aluminum, the reduction process of magnesium oxide by ferrosilicon was as follows: at 700~950℃, silicon participated in a reduction in the form of Al3FeSi2, and at 1200℃, the magnesium oxide was reduced in the form of Si and FeSi2. Under the experimental conditions, when aluminum participated in the reduction of magnesium by ferrosilicon, the reduction rate of magnesium oxide increased gradually with the increase of aluminum dosage. When the aluminum dosage was 12% and 1000℃, the reduction rate of magnesium oxide can reach more than 90%. Aluminum participated in the reduction of MgO to produce alumina, which reactd with CaO and SiO2 in calcined dolomite to produce CaAl2O4, CaAl2Si2O8.
    Role of surface energy in the formation of ice morphology
    Qinqin WU Yongjun CHEN Xianglei DONG Hui XING Yongsheng HAN
    Chin. J. Process Eng.. 2021, 21(4):  446-453.  DOI: 10.12034/j.issn.1009-606X.220110
    Asbtract ( )   PDF (3844KB) ( )  
    Related Articles | Metrics
    The icing phenomenon is ubiquitous in nature, from the formation of snowflakes to the low-temperature preservation of food to the anti-icing of aircraft wings. It is both a scientific and technological interest to understand and control the morphology of ice crystals. Inspired by the concept of mesoscience, this study raises the scientific hypothesis that surface energy plays an important role in the morphology evolution of ice crystals. To regulate the surface energy, different additives (sucrose, sodium chloride, and surfactant SDS) were added to the aqueous solution, and the icing processes with different surface tensions was observed by a homemade cooling device loaded at a laser confocal microscope. It was found that the morphologies of ice crystals transfer from dendritic with good symmetry to disordered seaweed crystals with the decrease of the surface tension at the same undercooling conditions, and this change was verified in different kinds of solutions. Further investigations showed that the lower surface tension of the solution resulted in a change of growth rate of ices in the solution. At high growth rates, the growing surface of ice crystals became unstable, and the crystal plane grew anisotropically, resulting in the formation of dendrite structures. However, at low growth rates, the growth surface of ice crystals was covered by additive molecules. The anisotropy of the crystal plane disappears, and hence a disordered dendrite structure was formed. The above findings confirmed the dominant role of supercooling and surface energy in the growth of the material structure, which provides experimental proof to evaluate the concept of mesoscience.
    Biochemical Engineering
    Preparation of submicron Pickering emulsion stabilized by cellulose nanocrystals
    Yanling QU Jie WU Guanghui MA
    Chin. J. Process Eng.. 2021, 21(4):  454-462.  DOI: 10.12034/j.issn.1009-606X.220141
    Asbtract ( )   PDF (1872KB) ( )  
    Related Articles | Metrics
    Compared with the traditional surfactant-stabilized emulsions, Pickering emulsions stabilized by solid particles have the advantages of strong interfacial stability, versatility, and low toxicity. A number of cases have demonstrated the potential of Pickering emulsions in biomedical applications. Submicron Pickering emulsion has a larger specific surface area and more efficient delivery efficiency than large-sized Pickering emulsions, which is expected to further expand the advantages of Pickering emulsions in the biomedicine fields. However, the size of Pickering emulsions is determined by many factors such as particle properties, characteristics of oil and water phase. And it is difficult to arrange the rigid particles in a limited and small oil–water interface. The above reasons increase the difficulty of preparing the submicron Pickering emulsions. The purpose of this study is to prepare stable submicron-sized Pickering emulsion by utilizing the natural polysaccharide with good biocompatibility-cellulose nanocrystals (CNCs) as particle emulsifier, squalene as oil phase. The effects of preparation conditions such as particle concentration, oil–water ratio, aqueous phase, ultrasonic time and frequency on size distribution and stability of Pickering emulsions were investigated. Finally, the submicron-sized Pickering emulsion (CNCs-PE) with good storage stability and centrifugal resistance was prepared, and the average size of CNCs-PE was about 638.7?8.40 nm. The confocal laser scanning microscopic (CLSM) images revealed that Pickering emulsion was formed successfully by the adsorption of CNCs on the oil–water interface. The cytotoxicity of CNCs and CNCs stabilized Pickering emulsion (CNCs-PE) was evaluated using CCK-8 method, and it showed that there was no significant loss of cell viability. In addition, the vaccine formulation was prepared by absorbing antigen protein-OVA. The adsorption efficiency of OVA was about 80%, and the histological micrographs of the intramuscular injection site section also showed the injection safety. It is expected to expand the applications of submicron-sized Pickering emulsion based on CNCs in biomedicine fields.
    Preparation and characterization of amphiphilic lipopeptide nanosuspension lyophilized powder
    Mengqiu ZHANG Huijuan JIN Fangling GONG Youhong ZHANG Yi WEI Yuxian HE Guanghui MA
    Chin. J. Process Eng.. 2021, 21(4):  463-470.  DOI: 10.12034/j.issn.1009-606X.220144
    Asbtract ( )   PDF (536KB) ( )  
    Related Articles | Metrics
    AIDS has spread widely and become a serious public health problem around the world. Membrane fusion inhibitor LP-98 shows strong antiviral activity among the anti-AIDS drugs under study in China, and has broad clinical application prospects. However, the clinical application of LP-98 is limited by its low solubility and poor suspension ability in aqueous phase, which could lead to blocked needle during injection and patient's pain. To improve solubility of LP-98, high-pressure homogenization technology was used to prepare LP-98 nanosuspension lyophilized powder (LP-98 NSLP). The optimal preparation process was as follow: the optimum stabilizer was sodium dodecyl sulfate (SDS), the concentration of SDS was 0.80wt%, the high-pressure homogenization pressure was 150 MPa, and it was repeated 5 times. The physical and chemical characterization and pharmacokinetics study of LP-98 NSLP were investigated. The LP-98 nanosuspension lyophilized powder had an average particle size of 261.5±1.1 nm and a Zeta potential of ?31.5±0.2 mV. Circular dichroism spectrometer and single-cycle virus infection experiments showed that the structure and biological activity of active pharmaceutical ingredients (API) were unchanged. The pharmacokinetic results showed that the bioavailability of the LP-98 NSLP was 98.1% of API. The solubility of LP-98 in water has been increased from 184 μg/mL to 1733 μg/mL, which was 8 times higher than that of the API. The drug activity in the LP-98 nanosuspension lyophilized powder was well preserved, and the solubility of the drug was improved. As a result it solved the problem of blocked needle during injection due to poor suspension of LP-98, hence reduced patient's pain. This research promoted the development of LP-98 application in clinical.
    Enzymatic hydrolysis of penicillin mycelium protein
    Zhan'ao ZHANG Qingfen LIU
    Chin. J. Process Eng.. 2021, 21(4):  471-478.  DOI: 10.12034/j.issn.1009-606X.220122
    Asbtract ( )   PDF (406KB) ( )  
    Related Articles | Metrics
    More than 2000000 tons of antibiotics fermentation residues (AFRs) were produced in China every year, which were hazardous solid waste, and how to safely dispose of them is attracting attention. AFRs are rich in organic substances, such as protein and carbohydrates, which accounts for about 50% of dry penicillin AFRs. So it is significant to develop new methods for recycling and utilization of mycelium protein in AFRs. In this work, penicillin mycelium was dissolved by alkali-thermal method, and penicillin mycelium protein solution was prepared, and then enzymatic hydrolysis performance of penicillin mycelium protein was explored in this solution using enzyme as catalyst, such as alcalase (A), bromelain (B), neutrase (C), and acid protease (D). The effects of types of enzymes, pH of the solution, the ratio of enzyme to protein, reaction temperature and time on protein hydrolysis process were systematically studied, and an optimization scheme was proposed. In a single enzyme-catalyzed hydrolysis process, alcalase showed the optimal performance, the hydrolysis degree of protein reached 31.43% at following conditions, the mass ratio of alcalase to protein as 6%, pH=11, the reaction time of 3 h and temperature of 50℃. In the complex enzyme-catalyzed hydrolysis process, the mixture of alcalase and bromelain as catalysts was demonstrated got the best efficiency. The optimum parameters were as follows: the mass ratio of complex enzyme to protein was 9% (A:B=2:1), pH=10, the reaction time of 3 h and temperature of 50℃. Under these optimal conditions, the protein hydrolysis degree reached 42.73%, which was 11.30 percentage points higher than the best single-enzyme method. The high performance liquid chromatography (HPLC) analysis found the enzymatic hydrolysate contained 16 amino acids, such as glutamic acid, aspartic acid, glycine, leucine and alanine, the ratio was 15.47wt%, 11.94wt%, 9.41wt%, 9.23wt%, 9.22wt%, respectively. This work provides a high efficient enzyme-catalyzed hydrolysis method of penicillin mycelium protein for preparing amino acids, and to carry out utilization of penicillin mycelium protein in AFRs.
    Environment & Energy
    Ionogel electrolyte based TiO2(B)@C/CNT//AC quasi-solid-state lithium-ion capacitors
    Bosen LI Jiahe ZHANG Lipeng YANG Jiajia LI Chunxian XING Haitao ZHANG
    Chin. J. Process Eng.. 2021, 21(4):  479-487.  DOI: 10.12034/j.issn.1009-606X.220150
    Asbtract ( )   PDF (1001KB) ( )  
    Related Articles | Metrics
    Lithium-ion capacitors (LICs) are attracting extensive attentions owing to their high energy density, rapid power output, and excellent cyclability. However, one of the key challenges encountered by LICs is balancing the sluggish kinetics of intercalation electrodes against capacitive electrodes. In this work, a TiO2(B)@C/CNT nanohybrid electrode was synthetized by a microwave-assisted solvothermal method. The nanohybrids exhibited a high reversible capacity of 291 mAh/g and high kinetic characteristics. Subsequently, a polyimide (PI) membrane was prepared by electrospinning technique for the construction of a ternary ionogel electrolyte. The ionogel electrolyte exhibited high ionic conductivity and electrochemical stability. Notably, a quasi-solid-state lithium-ion capacitor (QSLIC) was assembled with TiO2(B)@C/CNT as anode, commercial activated carbon (AC) as cathode and the ionogel electrolyte. It delivered a maximum energy density of 83.1 Wh/kg and a maximum power density of 18338.1 W/kg at 60℃. Moreover, the electrochemical performances of the QSLIC exhibited an obvious temperature dependence.
    Study of removing heavy metals from acid mine wastewater with solvent extracting system of Mextral V10–Mextral 973H
    Xiaohui LI Xianbin AI Yongming WU Xiaoyan SUN
    Chin. J. Process Eng.. 2021, 21(4):  488-494.  DOI: 10.12034/j.issn.1009-606X.219338
    Asbtract ( )   PDF (807KB) ( )  
    Related Articles | Metrics
    The mine drainage from mineral and metallurgical processing has complex composition and large amount of water. At present, the effect is not ideal and high cost of heavy metal removal method. In order to solve the problem of heavy metal pollution in mine drainage, a synergistic extraction method has been developed to remove and recover heavy metals from mine drainage, which could be used to the solution with the high acidity and low heavy metal concentration, and inhibit calcium and magnesium ions enter into extractant. A synergistic extractant of Mextral V10–Mextral 973H was obtained for the effective removal of Cu2+, Pb2+, Cd2+ and Zn2+ from the acidic wastewater by the analysis of metal extraction pH isotherms, FT-IR spectrum and UV–vis absorption spectra. The volume ratio of organic phase and water phase (O/A), the saponification rate of Mextral V10 and extracting agent concentration has been studied on the effect of metal ions extraction. The extractability percentage of Cu2+, Cd2+, Zn2+, Pb2+, Mg2+ and Ca2+ were 99.1%±0.1%, 99.9%±0.02%, 99.5%±0.05%, 97.6%±0.03%, 10.11%±0.1% and 18.3%±0.05% respectively after sixth extraction continuously under the optimum experimental conditions of 10vol% (Mextral V10 and Mextral 973H) diluted in Mextral DT100 and Mextral V10:Mextral 973H=1:1, the residual concentration of Cu2+, Zn2+, Cd2+ and Pb2+ in wastewater were 1.720±0.10, 0.256±0.03, 0.054±0.01 and 0.929±0.01 mg/L respectively, which were lower than the maximum allowable emission standard value of class Ⅰ pollutant in GB8978-1996.