ZSM5-Y型分子筛催化剂复配体系裂化性能数值研究

采用流动和反应耦合模型模拟ZSM5-Y复配催化剂体系在提升管反应器内的催化裂化过程。结果表明,重油催化裂化反应主要发生在喷嘴附近,该处有45%的重油转化为汽油和柴油。对于ZSM5-Y型复配催化剂体系,ZSM5加入沸石催化剂的显然影响着汽油和液化气的产率,反应产物中柴油馏分及重油馏分的产率基本上不受影响。加入少量择形催化剂便大大降低提升管反应器汽油馏分收率,并提高液化气收率,但汽油与液化气产率显著变化仅发生在择形催化剂加量较小的时候,一旦超过10%以后,对气油和液化气的产率影响反而较小。     

Numerical solutions of unsteady flows with low inlet Mach numbers

This study deals with a numerical solution of a 2D unsteady flow of a compressible viscous fluid in a channel for low inlet airflow velocity. The unsteadiness of the flow is caused by a prescribed periodic motion of a part of the channel wall with large amplitudes, nearly closing the channel during oscillations. The channel is a simplified model of the glottal space in the human vocal tract and the flow can represent a model of airflow coming from the trachea, through the glottal region with periodically vibrating vocal folds, and to the human vocal tract.     

16升气升式环流反应器优化设计的CFD仿真研究

以16L内循环气升式环流反应器为对象,使用Fluent6.3软件对采用不同导流筒直径值的反应器中气液两相流动的过程进行计算流体力学仿真,研究导流筒直径变化对气升式环流反应器中气含率和循环液速的影响。结果表明,气体由反应器底部入口进入反应器后,气液混合物沿导流筒内部上升至反应器顶部,随后沿导流筒外部下降,形成反应器中的循环。增大导流筒直径在一定范围内能够提高反应器中的气含率,但同时也会造成循环液速的下降,并且给出了所涉对象中导流筒直径的最优取值区间。     

Low temperature co-fired ceramic (LTCC)-based biosensor for continuous glucose monitoring

This article presents design, fabrication and testing of a miniature ceramic-based biosensor which is destined for continuous glucose monitoring. It is fabricated using well known LTCC (low temperature co-fired ceramics) technology. The biosensor consists of a microreaction chamber, three thick-film electrodes and a microdialysis tube. The detection process is based on oxidation of glucose by molecular oxygen in the presence of enzyme - glucose oxidase, GOx. One of the reaction products is a hydrogen peroxide which is detected amperometrically during its oxidation at a working electrode. Computational fluid dynamics (CFD) analysis was used for optimization of the biosensor geometry and considerations of the influence of operating conditions (flow rate) on mass transfer (diffusion) of the glucose within the microreaction chamber. Tests of the developed LTCC-based biosensor indicate its linear response to glucose concentration up to 9 mM with a relatively high sensitivity of about 147 nA/mM. Moreover, the properties of the presented ceramic biosensor are compared with properties of a similar device made in silicon/glass and in Perspex^®.     

微尺度射流流量计的设计与仿真研究

MEMS流量控制系统中,需要微型化的流量传感器,设计了一种反馈流驱动的微尺度射流流量计.采用数值模拟的方法对微尺度射流流量计进行研究,CFD软件的仿真结果表明:在较宽入口速度范围内该微尺度射流流量计起振快,振荡稳定,切换灵敏,斯特劳哈尔数基本恒定,并且流速测量下限可以达到0.075 m/s,在一定程度上为射流流量计的微...     

风机流场并行数值模拟在集群系统上的应用

介绍集群系统的特点及其软硬件配置环境。利用计算流体力学商用软件Fluent对一种新型垂直轴风力机风轮在曙光天潮超级服务器4000A集群上进行数值模拟及并行计算,得到风轮内外部的三维流场,实现该软件在高性能并行计算机上的应用,为并行有限元分析提供一个基础计算平台。     

SCR脱硝系统静态混合器优化布置数值模拟研究

基于CFD数值模拟技术系统地研究了静态混合器对改善SCR脱硝系统首层催化剂入口截面速度/浓度均匀分布特性的作用规律。数值计算结果表明,针对特定的静态混合器型式,优化前后速度/浓度分布偏差最大改善量分别为8.89%、12.26%,系统整体压损最大升高量约为188 Pa。因此认为静态混合器的优化布置可以显著改善截面内的速度/浓度均匀分布特性,但基于系统压损呈现的变化规律,建议在进行静态混合器设计时需综合权衡速度/浓度分布偏差改善性能与系统整体压损变化特性两方面的因素。     

基于CFD的摆线泵进出油腔对容积效率影响的分析

为提高摆线泵的容积效率,优化泵内部的流场分布,减少回流和空化现象.利用CFD方法对摆线泵内部流场进行数值模拟,定量分析月牙状进出油腔对泵容积效率的影响.仿真结果表明,适当减小G0并增大F0可以改善泵的内部流场分布,提高容积效率.仿真结果可以为摆线泵的结构设计提供参考.     

CFD方法在压水堆安全分析中的应用现状和发展趋势

为更好地利用CFD方法解决压水堆安全分析问题,简要介绍CFD方法,着重阐述其在硼稀释、混合和热分层以及受压热冲击等压水堆安全分析问题的应用现状,并提出CFD与系统程序的耦合计算、流固耦合计算和CFD与中子动力学程序的耦合计算将是CFD方法在该领域的发展重点.     

Computational performance of a parallelized three-dimensional high-order spectral element toolbox

In this paper, a comprehensive performance review of an MPI-based high-order three-dimensional spectral element method C++ toolbox is presented. The focus is put on the performance evaluation of several aspects with a particular emphasis on the parallel efficiency. The performance evaluation is analyzed with the help of a time prediction model based on a parameterization of the application and the hardware resources. Two tailor-made benchmark cases in computational fluid dynamics (CFD) are introduced and used to carry out this review, stressing the particular interest for clusters with up to thousands of cores. Some problems in the parallel implementation have been detected and corrected. The theoretical complexities with respect to the number of elements, to the polynomial degree, and to communication needs are correctly reproduced. It is concluded that this type of code has a nearly perfect speedup on machines with thousands of cores, and is ready to make the step to next-generation petaFLOP machines.