CFD studies on the separation performance of a new combined gas–solid separator used in TMSR-SF

In order to comply with discharge standards, a gas–solid separator is used to remove solid particles from the thorium molten salt reactor-solid fuel (TMSR-SF) system. As a key component, it directly determines system energy efficiency. However, current gas–solid separators, based on activated carbon adsorption technology, result in high pressure drops and increased maintenance costs. In the present study, a new combined gas–solid separator was developed for the TMSR-SF. Based on a simplified computational fluid dynamics (CFD) model, the gas–solid twophase flow and the motion trajectory of solid particles were simulated for this new separator using commercial ANSYS 16.0 software. The flow and separation mechanism for this structure were also been discussed in terms of their velocity effects and pressure field distributions, and then the structure was optimized based on the influence of key structural parameters on pressure and separation efficiency. The results showed that the standard k–ε model could be achieved and accurately simulated the new combined separator. In this new combined gas–solid separator, coarse particles are separated in the first stage using rotating centrifugal motion, and then fine particles are filtered in the second stage, giving a separation efficiency of up to 96.11%. The optimum blade inclination angle and numbers were calculated to be 45° and four, respectively. It implicated that the combined separator could be of great significance in a wide variety of applications.

Separation of Eu^3＋ Using a Novel Dispersion Combined Liquid Membrane with P507 in Kerosene as the Carrier

The separation of Eu^3 ＋is studied with a dispersion combined liquid membrane（DCLM）,in which polyvinylidene fluoride membrane（PVDF）is used as the liquid membrane support,dispersion solution containing HCl solution as the stripping solution,and 2-ethyl hexyl phosphonic acid-mono-2-ethyl hexyl ester（P507）dissolved in kerosene as the membrane solution.The effects of pH value,initial concentration of Eu3 ＋and different ionic strength in the feed phase,volume ratio of membrane solution to stripping solution,concentration of HCl solution, concentration of carrier,different stripping agents in the dispersion phase on the separation are investigated.The optimum condition for separation of Eu3 ＋is that concentration of HCl solution is 4.0 mol·L 1,concentration of carrier is 0.16 mol·L 1,and volume ratio of membrane solution to stripping solution is 30︰30 in the dispersion phase, and pH value is 4.2 in the feed phase.The ionic strength has no significant effect on separation of Eu3 ＋.Under the optimum condition,when the initial concentration of Eu3 ＋is 0.8×10 4mol·L 1,the separation percentage of Eu 3＋is 95.3%during the separation time of 130 min.The kinetic equation is developed in terms of the law of mass diffusion and the theory of interface chemistry.The diffusion coefficient of Eu3 ＋in the membrane and the thickness of diffusion layer between feed phase and membrane phase are obtained and their values are 1.48×10 7m 2·s 1and 36.6μm,respectively.The results obtained are in good agreement with literature data.

A new technique of combining accretion by cyclone separator and scattertube for tailings dams

A new technique of combining accretion by cyclone separator and scattertube for tailings dams was developed according to laboratory experiment, model experiment and spot experiment technology. Three tailings dams were successfully constructed by the new technique. The results of engineering geological exploration, static and dynamic test and stability analysis on Baizhishan tailings dams prove that the new technique improves structure and stability of the dams and working conditions compared with the traditional technique. The thin layers of fine-grained soils are greatly reduced, fine tailings sand is solid to make the dam stable and seepage conditions are well improved; the immersing line of the dam descends. In addition, the stability and liquefaction resistance of tailings dams are strengthened remarkably. The interior stress is compressive stress, stress level of every element is less than 1.0 and safety coefficient of every element is greater than 1.0. The safety coefficient against liquefaction of every element of tailings dams is greater than 1.5 according to the analysis of seismic response by finite element method.

New Technologies of Combined Agglomeration-separationfor Wolframite Fines

The new technology of combined agglomeration-separation and conditions for treating wolframite fineswere discussed. A mixture of wolframite and four kinds of gangue fines (quartz , fluorite, garnet and calcite)can be separated by this new technology. At high feed grade (wolframite : gangue = 1: 1) , wolframite con-centrate obtained by sedimentation assays 6 1 . 22 % ￣ 68. 33 % WO_3 with a recovery of 84. 4 % ￣93. 4 %. Atlow feed grade (wolframite : gangue =1 : 5) , wolframite ocncentrate obtained by combined agglomeration-separation and low-intensity magnetic separation assays 51 . 5% WO_3 with a recovery of 92. 0%. The majorfactors influencing these processes are the dosage of reagents and magnetite used, the time and the speed of agitation.

Hydrate-based carbon dioxide capture from simulated integrated gasification combined cycle gas

The equilibrium hydrate formation conditions for CO2/H2 gas mixtures with different CO2 concentrations in 0.29 mol% TBAB aqueous solution are firstly measured.The results illustrate that the equilibrium hydrate formation pressure increases remarkably with the decrease of CO2 concentration in the gas mixture.Based on the phase equilibrium data,a three stages hydrate CO2 separation from integrated gasification combined cycle （IGCC） synthesis gas is investigated.Because the separation efficiency is quite low for the third hydrate separation,a hybrid CO2 separation process of two hydrate stages in conjunction with one chemical absorption process （absorption with MEA） is proposed and studied.The experimental results show H2 concentration in the final residual gas released from the three stages hydrate CO2 separation process was approximately 95.0 mol% while that released from the hybrid CO2 separation process was approximately 99.4 mol%.Thus,the hybrid process is possible to be a promising technology for the industrial application in the future.

Produced-water treatment: Application and research of combined fiber coalescence technique in offshore oilfield

When the process of extraction of oil from an offshore oilfield enters the advanced stages,the water content in the extracted fluid can be above 90%.The water quality is complex with many types of pollutants and highly emulsified water.Therefore,a key consideration in the production process of offshore oilfields is the efficient and economical treatment of the oil-containing produced water to make it suitable for discharge and recover oil pollutants.In this study,we developed a hydrophilic and hydrophobic combined fiber coalescence separator with composite fiber shapes using fiber induction and X/Uweaving.The separator is designed based on experimental observations of the mechanism of structure coalescence in the physical oil removal method.A pilot test was performed on an oil exploration platform in the Bohai Sea.At the designed flow rate,the separator reduced the total concentration of petroleum in the produced water from 2000 to 3000 mg/L to below 60 mg/L,with an average oil removal efficiency of 98.24%.Furthermore,it effectively reduced the number of organic compounds present in the water from 120 to 17 and removed 70% of the SS.The test results show that the proposed device can be used fr produced-water treatment on offshore platforms.

Exact Solutions to a Combined sinh-cosh-Gordon Equation

Based on a transformed Painlev~ property and the variable separated ODE method, a function transfor- mation method is proposed to search for exact solutions of some partial differential equations （PDEs） with hyperbolic or exponential functions. This approach provides a more systematical and convenient handling of the solution process of this kind of nonlinear equations. Its key point is to eradicate the hyperbolic or exponential terms by a transformed Painleve property and reduce the given PDEs to a variable-coefficient the resulting equations by some methods. As an application, are formally derived. ordinary differential equations, then we seek for solutions to exact solutions for the combined sinh-cosh-Gordon equation

Development of Combined Biological Technology for Treatment of High-strength Organic Wastewater and Results of Case Studies

Our study group has developed a unique combined ters from the industries of dyestuff, pharmaceutical, chemical biological technology to treat high-strength organic wastewaengineering and zymolysis by using the principles of anaerobic ecological niche and bio-phase separation. The study obtained five national invention patents and eight patent equipments. This technology contains four kernel processes - two-phase anaerobic-aerobic process, hydrolysis-acidification-oxidation process, UASBAF-oxidation process, and internal cycling-hydrolysis-oxidation process. Fifteen pilot projects were accomplished in the basins of Tai Lake, Huai River, Liao River and Songhua River, and their total capital investment reached 185.214 million Yuan （RMB）. Compared to conventional wastewater treatment technology, the innovative technology is more costeffective for high-strength organic wastewater treatment, can save capital investment by 15% - 30%, lessen land usage by 20% to 40% and decrease the operating cost by 10% to 25%. The operating cost of treatment per cubic meter industrial wastewater could be below 0.6 to 1.4 Yuan （RMB）.

Parameter matching and experiment of the combined cyclone separation and cylinder sieve cleaning system for rape combine harvester

Existing rape combine harvester with a cyclone separation cleaning device has the challenge that the loss rate and the cleaning rate increase and decrease simultaneously.A cleaning process route was proposed,which involves the cyclone separation cleaning device removing light and tiny impurities,and the cylinder sieve device removing coarse and long impurities such as pod shells and short stems.A novel cleaning system combining the cyclone separation cleaning device and cylinder sieve cleaning devices was designed.The ranges of the structure and operation parameters for each component were analyzed based on kinematics and dynamic analysis.A four-factor five-level quadratic orthogonal test was carried out,in which the loss rate and cleaning rate were taken as the evaluation indexes.The velocity at the suction port,the rotation speed of the cylinder sieve,the screw pitch of the spiral blade and the diameter of the sieve hole were taken as the influencing factors.The orthogonal test results showed that the cleaning system performed best at a rotation speed of the winnower is 600 r/min,an airflow velocity at the suction port is 18.25 m/s,a rotation speed of the cylinder sieve is 87 r/min,a screw pitch of the spiral blade is 440 mm and a diameter of the sieve hole is 4.48 mm.At this time,the loss rate of the cleaning system is 3.22%,and the cleaning rate is 95.67%.Compared to the conventional cyclone separation cleaning device,the loss rate is reduced by 2.17%and the cleaning rate is increased by 1.05%.This study can provide a reference for the optimal cleaning system design for rape combine harvesters.

Numerical study on the separation and superposition of the influences from up-and downstream rotors

A three-dimensional Navier-Stokes solver is used to investigate the separation and superposition of the influences from upstream and downstream rotors in an axial-radial combined compressor for unsteady design applications. The data from rotor/stator and stator/rotor configurations show that the unsteady flow response in axial stator passage is caused only by one rotor. The results from the rotor/stator/rotor configuration revealed the superimposed characteristic of influences from upstream and downstream the rotor. The impact of the superimposed characteristic was studied by analyzing the virtual relative flow angle at the stator exit. The results show that the axial velocity in the passage of axial stator can be influenced by wake from upstream axial rotor and potential field of downstream radial rotor. While they are coupled to have an effect on the unsteady flow in axial statot passage, the excitation or suppression phenomena appear and lead to different levels of deterministic fluctuation kinetic energy. Their locations are determined by the frequencies of the involved influences. In addition, the variability of superimposed characteristic （ excitation and suppression） at the stator exit modulates the inlet flow angle for downstream rotor.

油水分离技术的研究进展

综述了含油废水的定义､油的存在形态､油水分离技术以及吸油材料的研究进展。油水分离技术包括物理分离法､化学分离法､物理化学分离法以及组合工艺等。阐述了各种油水分离技术的基本原理､流程和特点,综合比较分析发现,应依据含油废水中油品的性质及存在形式选择合适的油水分离技术,并且兼顾经济效益。组合工艺是油水分离的发展趋势;高性能低成本油水分离材料以及油水分离设备的研发是未来油水分离技术发展的重点。

国产首颗全电推进通信卫星星间分离安全性设计

亚太6E卫星是国产首颗全电推通信卫星,也是全球首颗从低地球轨道到地球同步轨道实现全自主轨道转移的通信卫星。亚太6E卫星首先利用独立推进舱的化学推进系统实现快速轨道提升,接着卫星与独立推进舱分离,最终由卫星的全电推进系统完成后续轨道转移任务。星间分离是决定任务成败的关键,首先介绍亚太6E卫星星间连接与分离机构设计,接着依次对连接应力裕度、分离过程近场安全与远场安全开展分析,系统阐述全电推进平台搭配低成本运载火箭工程实践的经验与成果,对后续项目具有一定的参考意义。

环境放射性样品中锕系核素组合分离方法研究进展

环境放射性样品中锕系核素的准确分析依赖于可靠的化学分离。锕系组合分离是一种快速分离方法,具有同时分离多种核素、提高样品利用率,减少试剂用量和废物产生量等显著优势,成为锕系分析化学的研究热点。本工作综述了锕系核素分离方法及各方法的组合使用,以及自动化分离在锕系组合分离中的应用现状,并重点介绍了基于萃取色谱法的锕系组合分离研究进展。在此基础上,指出建立锕系核素组合分离方法面临的问题,并对该领域的发展趋势进行了展望。

最优尺寸参数对涡流管能量分离效应影响的研究

为确定出涡流管各因素的主次顺序,找出最优的参数组合,提出正交试验设计和极差分析法,找到涡流管能量分离效应的最优化尺寸参数。实验设定涡流管进气温度为26℃,环境温度为27.1℃,结果表明,4个尺寸参数对涡流管能量分离影响排序为:长径比>喷嘴数目>冷端直径>进气压力,每个参数的最优值各为长径比为25.0、喷嘴个数为6、冷端直径为5 mm、进气压力为0.8 MPa,并通过对试验结果的验证,发现涡流管的冷热端出口温差为95.2℃。根据正交试验设计方案找出了涡流管各部件的最优尺寸参数。

“分合协同”药学硕士专业学位研究生创新人才培养途径探索

针对“新医科”建设背景下药学硕士专业学位研究生培养要求,南京医科大学秉持采用“需求-培养-发展”培养理念,从培养体系、培养环境和培养手段等方面,探索药学硕士专业学位研究生“分合协同”培养途径,在践行药学硕士专业学位研究生培养过程中取得了一定成效。

内蒙古白云鄂博某低品位含铁岩矿磁悬浮联合分级流程工业试验研究

白云鄂博铁矿石储量巨大,缓解了国家铁矿石对外依存度过高的问题,同时也助力了包钢集团生产发展。但是在采矿过程中,产生了大量TFe品位低于20%的低品位含铁岩矿。对该类矿石,采用传统连续磨矿-磁选流程,在细磨至-0.074 mm粒级含量95%情况下,铁精矿品位最高只有60.8%,无法达到合格铁精矿质量要求;如果采用浮选流程,选矿经济性能不佳,故该部分矿石一直进行堆放未得到应用。本文通过对原矿性质进行分析,引入新型磁悬浮精选机作为磁选精选设备,同时设计三条全磁工艺流程进行工业试验,均可得到TFe品位64.5%以上的合格铁精矿,同时铁精矿中杂质元素K、Na、Si含量远低于浮选工艺流程。其中,自主开发的阶段磨选-磁悬浮联合分级分选流程,在细磨至-0.074 mm粒级含量95%情况下,最终可得到铁精矿TFe品位64.5%、磁性铁回收率95.07%的优良技术指标,分选效率高,效果好。现场应用后可实现白云鄂博低品位含铁矿经济性绿色利用,经济效益显著,同时极大地延长了白云鄂博铁资源的供给年限,对国家自有铁矿石产能接续、矿山自身可持续发展及资源绿色利用具有深远意义。

金矿选矿技术研究进展

为助力国内金矿选矿技术攻关,实现金矿资源的高效、合理化开发利用,通过梳理国内金矿资源分布情况及典型黄金矿山的重选法、浮选法、联合工艺和预处理选矿工艺的研究现状,针对性地总结了含碳高砷、高硫、难处理金矿的研究方向,为实现难选金矿资源的高效、合理化开发利用提供了思路。

论庄子形神分合思想

庄子思想中的形、神关系并非一成不变:当庄子逍遥于理想世界时,他强调形神之分,追求剥离形体后的精神绝对自由;当他跌落现实世界以后,又不得不强调形神之合,主张二者并重,形神兼养。庄子这一形神分合思想对后世文人、道教、佛教等都产生了广泛深远的影响。认真梳理庄子这一主张,不仅有利于进一步深刻理解庄子思想,对今天的现实生活也具有一定的借鉴意义。

含磁黄铁矿型硫铁矿选矿技术研究

内蒙古某硫铁矿含硫23.66%、含铁32.26%,为了开发利用该矿产资源,对其进行原矿性质研究和选矿技术研究。原矿性质研究表明,该矿石主要金属矿物为黄铁矿,其次是磁黄铁矿和磁铁矿;脉石矿物主要为白云石和方解石。试验确定的原则工艺流程为“浮选-磁选”联合流程。当磨矿细度为65%-0.074 mm,硫酸铜用量为300 g/t,丁基黄药用量为230 g/t,2^(#)油用量为60 g/t时,原矿经过一次粗选、一次扫选和两次精选产出硫精矿,闭路试验获得硫精矿中硫品位为43.42%,硫回收率为85.46%;在粗选磁场强度为1300 Oe、精选磁场强度为800 Oe条件下,进行一次粗选一次精选,最终获得铁精矿中铁品位为53.76%,铁回收率为17.55%的选矿指标。

基于移动端的方药离合实训平台设计与实现

针对中医药高等院校学生在学习方剂学过程中存在的知识点众多、识记量大、兴趣度不高和日常练习困难等问题,通过调研分析,设计一种基于Unity仿真技术的移动端方剂学方药离合实训平台。该平台前端主要采用Unity框架构建功能模块,选取JWT进行轻量级身份验证,并应用RBAC思想实现权限管理;后端业务逻辑在使用SpringBoot框架的基础上,通过Java语言编写。为了保证系统响应速度及交互效果,融合MySQL、Redis、ElasticSearch三种体系架构的优点,构建了一套性能高效且便于移植的数据库机制。所设计平台实现了知识点内容学习、笔记收藏、错题集、方剂分类练习、用户在线PK、积分排行榜等功能。经过中医药相关专业学生的验证及使用,验证了该平台能够有效地利用碎片化时间,随时随地学习和测试用户对于方剂学知识的掌握情况,达到了提高自身学习效率的目的。