Gas-solid separation performance and structure optimization in 3D printed guide vane cyclone separator

Low separation efficiency and large pressure drop are two common problems of cyclones. In this paper, a 3D printed guide vane cyclone separator was designed to study the separation efficiency, turbulent kinetic energy, and particle movement of particle group by experiment and simulation. The results shown that the tangential velocity was the major influence of separating. The bottom of the exhaust pipe was the main region of gas–solid separation and pressure drop. The separation efficiency and pressure drop were positively correlated with the inlet velocity and the particle radius of the fluid. The distribution of turbulent kinetic energy that leaded to the pressure drop loss was concentrated on the inlet of the exhaust pipe. The swirl has external and internal two directions. The optimized cyclone has a longer and narrower blade flow path to obtain higher separation efficiency, especially at low inlet velocity.     

基于fluent的旋流器分级控制系统设计

目前,应用重介旋流器分选过程智能控制策略、极群组破碎分离水力旋流器参数化方法局限于单参数优化,难以控制微小尺寸变形,基于该问题,设计了基于fluent的旋流器分级控制系统。使用开关型交流稳压电源,为系统提供可靠电能。利用Q941F电动调节球阀,执行对应区间动作。使用BST6800系列压力变送器,实现底流流量控制。采用上装式气动阀门开关结构,增强阀门可靠性。通过人机交互模块,显示执行任务。根据基于fluent的数值模拟原理,计算进入旋流器的颗粒直径。结合Gambit模型和网格划分方法,仿真模拟分析切向速度、横向速度和径向速度三个方向分量分布情况。使用两套控制输出量调节旋流器进料速度,获取最佳分级尺寸,保证旋流器分级过程的稳定性。由实验结果可知,该系统最高分级效率为98%,最低为90%,具有高效分级效果。     

NUMERICAL SIMULATION OF SWIRLING FLOW IN A CYCLONE CHAMBER

The ability to predict the influence of design parameters on the aerodynamics of cyclone chambers flows is of prime concern in furnace engineering and a number of high temperature processes. The two-dimensional Los Alamos SOLA prediction technique has been extended to include the computation of an axisymmetric swirling flow. The transient Navier-Stokes equations of an incompressible fluid are solved via their associated finite difference equations, directly in terms of the primitive pressure-velocity variables. For this, a short simple computer code has been developed, using a laminar flow simulation with 'free slip' wall boundary conditions. Predictions show that a useful characterization of the flowfield is now available. The simplified code represents a basic tool, to which user-oriented complexities and sophistications can be added later as required     

旋风分离器的快速设计方法

在理论研究和设计实践的基础上,提出了旋风分离器的快速设计 方法。该设计方法较简便实用,对旋风分离器的设计和实验具有指导 作用。     

中下游式尾矿坝设计概要

简要介绍了中、下游尾矿坝的特点、堆筑方法及设计中必须考虑的主要问题,并论述了主要技术指标的确定原则和方法。     

切流式旋风分离器的结构对颗粒分离的影响

切流式旋风分离器以其结构简单、成本低廉、制造方便,又可耐高温、高压而广泛地应用于石油、化工、冶金、食品、医药等行业中,用于气固相分离,特别是去除含尘气相物料中的粉尘颗粒以及熔炼炉、干燥器的尾气除尘。     

新型无砂仓尾砂胶结充填工艺技术

近年来利用选厂尾砂进行井下胶结充填的采矿方法在大中型地下铁矿山得到广泛应用,其尾砂胶结充填系统主要由立式砂仓和两级活化搅拌机组成,系统占地面积大,结构复杂,投资和运行费用较高。刘塘坊铁矿结合自己矿山的实际情况,利用本矿选厂尾砂进行旋流器浓缩实验研究,并使用自动化智能控制系统,研制、开发出一套低浓度无砂仓尾砂浓缩充填系统,在工业实践中应用,取得较好效果。通过工业实践,选厂尾砂利用率达到70%以上,尾砂浓缩浓度达到65%~70%;旋流器溢流实现自流进入尾矿库。整个充填系统实现远程集中控制,所有设备无需现场人工操作;应用智能加灰系统,精确控制充填所需灰比和浓度;通过故障自动判断和控制系统,实现了尾矿充填系统输送和尾矿库输送的自动切换。该系统占地面积小,结构简单,管理方便,投资、运行费用低,对于一些中小型地下矿山来说,具有一定借鉴价值。     

旋风除尘器内三维流场的数值模拟

文中建立了用于旋风除尘器模拟的计算模型,并数值模拟了旋风除尘器内部的流场运动情况,预测了复杂流场中影响颗粒分离效率的因素,为旋风除尘器流动机制的研究和进一步结构优化设计提供了参考依据.     

基于FPGA的PCIe接口实现

PCI Express是一种高性能互连协议,被广泛应用于网络适配、图形加速器、网络存储、大数据传输以及嵌入式系统等领域。文中介绍了PCIe的体系结构,以及利用Altera Cyclone IV GX 系列FPGA实现PCIe接口所涉及的硬件板卡参数、应用层系统方案、DMA仲裁、PCIe硬核配置与读写时序等内容。     

Design and performance of a pressurized cyclone combustor (PCC) for high and low heating value gas combustion

The combustion difficulties for low heating value (LHV) gases derived from biomass fuels via a gasification process have led to more investigations into LHV gas combustors. Cyclone combustors provide good air/fuel mixing with long residence times. In this study, a small-scale pressurized cyclone combustor (PCC) was designed and optimized using computational fluid dynamics (CFD) simulation. The PCC, along with a turbocharger-based, two-stage microturbine engine, was first characterized experimentally with liquefied petroleum gas (LPG) fuel and then with both LPG and LHV gas derived from biomass in dual-fuel mode. The combustor achieved ultra-low CO and NO_x emissions of about 5 and 7 ppm, respectively, for LPG fuel and of about 55 and 12 ppm, respectively, in dual-fuel mode at the maximum second-stage turbine speed of 26,000 rpm with stable turbine operation.