闪速固液分离装备技术浅析

针对云南澜沧铅矿NZ - 12浓缩机停用问题 ,充分利用原装备条件下 ,采用闪速固液分离装备技术 (旋流器同浓密机联合 ) ,变一段固液分离作业为二段固—固、固—液分离作业 ,使浓密机内固体负荷减少 5 0 %,粒度 <40 μm;采用高分子塑料减少耙径 2 5 6m ,使浓密机运行扭矩减少 40 %。在不增加运行成本情况下 ,成功把普通浓密机改造为高效浓密机。三年多的生产实践表明改造方案是先进、可靠、稳定、高效的。     

Influence of the adjustable vane position on the flow and combustion characteristics of a down-fired pulverized-coal 300 MWe utility boiler

Experiments with a small-scale cyclone burner used for burner enrichment in a down-fired pulverized-coal 300 MW_e utility have been conducted on an air/particle test facility. Particle separating efficiency was obtained with different positions of an adjustable vane. Industrial experiments were performed on a full-scale boiler. The gas temperature distribution along the primary air and coal mixture flow, gas temperature distribution of the furnace, and gas components such as O₂, CO, CO₂ and NO_X in the near-wall region were measured for the first time. The influence of the adjustable vane position on coal combustion in the furnace was determined. With the adjustable vanes at the nozzle, ignition of the primary air and pulverized-coal mixture was delayed and the gas temperature peak was above the burner arch, with high NO_X emission. Raising the vanes can bring forward the ignition point but results in the fuel-rich flow being up ahead of time, leading to a rise in carbon content in fly ash and NO_X emission.     

基于CycloneⅡ系列FPGA的DDFS信号源实现

直接频率合成技术为目前各种不同类型信号源设计的主要技术,本设计以QuartusⅡ为开发环境,利用VHDL语言,完成了正弦信号源的前端设计。并在CycloneⅡ系列EP2C35芯片上,不扩展外部存储器,时钟频率为40MHz的情况下,单片实现了频率步进为78Hz．频率范围为78Hz-1．25MHz的正弦信号源。     

干燥系统中的旋风分离器及半干法旋风除尘技术

比较了国内外常用的旋风分离器的结构尺寸和性能差别。利用干燥尾气中的水分,适当冷却尾气使相对湿度日在38％-45％的范围内,促使粉尘团聚成较大颗粒,从而使旋风分离器尾气排放中的小颗粒（dc≤3μm）的数量下降,提高了除尘效率,且除尘后的颗粒是干态的。半干法除尘比湿法除尘能节约用水和循环水的电能,同时可以避免在循环水中生物质的发酵变质。     

Effects of the prolonged vertical tube on the separation performance of a cyclone

This article aims at the gas flow into the dustbin of conventional cyclones, the prolonged cyclone (attaching a vertical tube at the bottom of the dust outlet) is proposed by some researchers, which can make flow with dust enter into the tube and separate further. The Reynolds stress transport model (RSTM) has been employed to predict the gas flow fields of the conventional and prolonged cyclones. The tangential velocity, axial velocity profiles and turbulent kinetic energy profiles are presented, and the downward flow rates into the dustbin of the three cyclones are compared. The separation performances of these three cyclones are tested. The result indicates that the tangential velocity, axial velocity and turbulent kinetic energy in the dustbin reduce greatly when the prolonged vertical tube attaching into the dust outlet, which can avoid the re-entrainment of already separated dust effectively. Furthermore, the prolonged vertical tube increases the separation space of dusts. The downward flow rate into the dustbin of the prolonged cyclone decreases compared with the conventional cyclone. The experimental results show that the prolonged vertical tube can improve the separation efficiency by a slightly increased pressure drop. However, for an even longer tube, the separation efficiency is slightly reduced. Thus, there is an optimal tube length for a given cyclone.     

循环流化床锅炉旋风分离器内气固两相流动的数值模拟

为研究旋风分离器内部气固两相流动的特征,应用FLUENT5.4.8软件对某厂50 MW级别的旋风分离器内部气固两相流动进行了数值模拟.在此基础上,又分别对中心筒长度减半、变梯形入口为弧形引导入口、增加筒径的3种改进模型重新进行计算,并得出有用的结论.这些数值模拟的结果对新型旋风分离器的设计、运行和改造等均具有指导意义.图32表2参3     

基于ARM＋FPGA的终端重配置硬件平台实现

介绍了基于ARM和FPGA的端到端重配置终端的硬件平台设计方法。给出了系统设计的硬件结构和重要接口,提出了由ARM微处理器通过JTAG在系统配置FPGA的方法,以满足重配置系统中软件的灵活性要求。并详细介绍了JTAG在系统配置FPGA的时序要求。     

排尘口直径对旋风分离器壁面磨损影响的数值模拟

基于计算流体动力学(Computational fluid dynamic,CFD)的数值模拟方法,在FLUENT软件平台上,应用雷诺应力模型、离散相模型和磨损值计算模型系统地研究排尘口直径对旋风分离器壁面磨损的影响。计算结果表明,旋风分离器壁面磨损的整体变化趋势不随排尘口直径的改变而变化,都呈现局部磨损的形态。排尘口直径减小,环形空间壁面磨损值保持不变,分离空间壁面磨损值有不同程度的增加,在锥体末端附近增加幅度最大,而这种变化主要是由于排尘口直径变化后分离器内部流动结构的变化引起的。分离空间锥体末端附近壁面的严重磨损主要受气固两相的旋转速度、颗粒浓度、旋进涡核和颗粒受力情况的影响。通过研究揭示合理地进行结构设计在减少磨损中的重要作用,为旋风分离器壁面的防磨提供数值试验方法和依据。     

Performance evaluation of industrial large-scale cyclone separator with novel vortex finder

This paper presents an experimental and numerical study on an industrial large-scale tangential-inlet cyclone separator with a novel and easy-to-implement vortex finder. The vortex finder was designed with slots on the side wall to improve cyclone performance. The collection efficiency, pressure drop, and interior flow field were analyzed. The proposed device provides an effective gas flow pathway and a coupled swirl-inertia separation mechanism, which eliminates short circuit flows under the bottom inlet of the slotted vortex finder to reduce the swirling intensity and minimize the flow instability in the separator. The pressure drop was reduced up to 27.9% compared to the conventional separator and the maximal increase in collection efficiency was 5.45%. The results presented here may provide a workable reference regarding the effects of vortex finders on improving flow fields and corresponding performance in industrial large-scale cyclone separators.