粉体性能对浓相气力输送特性的影响

气力输送过程中物料性能是确定输送特性的重要因素,因此,粉料气力输送技术的实现要以对粉料的性能研究为基础。文中对影响气力输送的粉体基本性能及其相关参数做了较全面分析,其中粒子尺寸、粒径分布、形状是影响粉料是否可适用于浓相气力输送的关键参数,其它特性都与这3种特性相关联。介绍了几种应用广泛的粉料气力输送特性分组方法,并进行了简要评述,同时指出了今后的研究方向。     

粉体性能对浓相气力输送特性的影响

气力输送过程中物料性能是确定输送特性的重要因素．因此．粉料气力输送技术的实现要以对粉料的性能研究为基础．文中对影响气力输送的粉体基本性能及其相关参数做了较全面分析．其中粒子尺寸、粒径分布、形状是影响粉料是否可适用于浓相气力输送的关键参数．其它特性都与这3种特性相关联。介绍了几种应用广泛的粉料气力输送特性分组方法．并进行了简要评述．同时指出了今后的研究方向。     

正压浓相恒压输送系统的DCS控制设计及应用

正压浓相气力输送系统是目前国内火电厂应用最为广泛的气力输送系统,该系统对运行的控制流程要求高、逻辑性强;其关键输送技术指标均采用模拟量进行检测,并实时控制.本文介绍的恒压输送系统,除了以上特点外,其独具的输送压力的动态实时调控功能,更是对控制系统提出更高的要求;阐述了DCS用于正压浓相恒压输送系统的典型设计.     

汉瑞普泽粉粒体技术(上海)有限公司

正产品名称:气力输送系统产品简介:固体物料气力输送是利用一定压力和速度的气流作为动力和载体,通过管道将粉、粒状固体物料搬运输送到指定地点的技术,广泛应用于化工、冶金、食品、医药等行业粉粒料的输送。气力输送具有清洁、快速和定量等优点。该技术不仅可输送粉状、粒状和纤维状物料(如聚乙烯、聚丙烯、PVC、谷物、棉花、炭黑等),还可输送小块状物料(如煤、岩石等)。可以气力输送的粉粒料品种繁多,每种物料的料性对气力输送装置的适合性和效率都有很大的影响。因此在选定输送装置     

石灰长距离气力输送系统的试验研究

基于气力输送理论,通过石灰的长距离输送试验系统的建立,研究输送过程中耗气量、管道压力损失、物料输送前后的状态等重要输送特性。结果表明,将气力输送应用在长距离的石灰输送上是完全可行的,可解决钢铁行业的高粉尘污染问题,极大地改善工作环境。     

量纲和谐原理在聚丙烯酰胺水平管段流动中的应用

以聚丙烯酰胺为研究对象,在自行设计气力输送系统上,结合量纲和谐理论,分析了水平管段沿程阻力系数的影响因素,及各影响因素之间的关系。结果表明:在水平管段中,利用量纲和谐原理得到的规律与试验过程中直接观察到的试验现象吻合,证明量纲和谐原理可以应用于聚丙烯酰胺在水平管道中流动及阻力特性试验研究中。在聚丙烯酰胺水平管段浓相输送中,影响沿程阻力系数的各参数的指数与物料的质量流量存在线性关系,这个结论为今后聚丙烯酰胺的气力输送提供了有力的理论依据。     

炭黑在气力输送系统中的破碎原因的分析

分析了炭黑在气力输送过程中的破碎机理。通过实验,介绍了气力输送系统中炭黑的种类和炭黑的物性对炭黑的破碎的影响,指出气力输送系统的输送管路长度和布置以及输送参数如输送压力和输送速度等的变化直接影响着炭黑的破碎率的大小。为更好地解决炭黑在气力输送中存在的问题,优化炭黑气力输送系统的设计提供了依据。     

炭黑在气力输送系统中的破碎原因的分析

分析了炭黑在气力输送过程中的破碎机理．通过实验．介绍了气力输送系统中炭黑的种类和炭黑的物性对炭黑的破碎的影响．指出气力输送系统的输送管路长度和布置以及输送参数如输送压力和输送速度等的变化直接影响着炭黑的破碎率的大小．为更好地解决炭黑在气力输送中存在的问题,优化炭黑气力输送系统的设计提供了依据．     

低能耗粉体物料气力输送的方法

粉体物料的输送有多种方式,采用管道气力输送是最经济环保的输送方式之一。对于长距离粉体物料气力输送,正压浓相加分段变径的设计思路是降低能耗/延长输送距离和减少管道磨损的最直接方法。     

气力输送粉煤灰固相浓度的超声检测研究

为了得到不同气力输送条件下管道内的固相浓度,以压缩空气为输送载体,以干燥粉煤灰为输送物料进行气力输送实验,利用低频超声测试系统对气力输送不同浓度的粉煤灰进行超声衰减测试,并选取合理的衰减信号处理模型。结果表明,在气力输送初始阶段,粉煤灰浓度会随着表观气速的增大而增大,随着输送进程的继续,发送仓泵内的物料减少,使得管道内粉煤灰浓度减小。     

Horizontal pneumatic conveying: a 3d distinct element model

Pneumatic conveying is widely used for transporting bulk solids in chemical, process and agricultural industries. It is environmentally friendly, flexible and can be fully automated. But it can also involve high power consumption, wear, abrasion, blockage and particle degradation. Hence understanding the physics can help to optimise design and operation. Conveying in a horizontal pipe involves complex multiphase flows, potentially with lean and dense phase regions, stationary particles and blockage.The Distinct Element Method (DEM) is a powerful tool to study granular dynamics. It models interactions at the particle level and reproduces the assembly physics. This paper presents a 3D DEM model to predict pressure drop, flowrate and flow patterns in pneumatic conveying. The inter-particle forces are modelled using the spring-dashpot-slider analogy. A novel gas flow model is developed. The pipe is divided into sections. In each section a lean and dense region is determined on a voidage criterion based on particle positions. Given the pressure at the boundaries, the fluid flow is determined assuming steady state conditions. This uses the Ergun equation for the flow through the dense phase and the equations of Wen and Yu for modified single spheres and wall resistance for the lean phase. It uses an iterative algorithm adjusting the fluid flowrate so that the pressure in each section is the same in the dense phase and lean phase and maintaining the boundary pressures. Once the fluid flow profile has been calculated the fluid drag on each particle can be determined. The results compare well with experimental data relating pressure gradient and solid and gas flowrates from Molerus (1993), Molerus (1996). Flow patterns for all the flow regimes, fully suspended flow, strand flow, slug flow, and conveying over stationary layer are observed.     

密相气力输灰管道的设计与应用

对气力输灰工程中密相输灰管道的设计和计算确定管内压力和速度的公式进行整理 ,同时可以得到较合理的管径和不同管径的长度。运行参数当已知时 ,给出的计算公式可作为设计的依据     

密相气力输送系统中几种气量控制方式的比较

从调压范围、压力特性和流量特性方面介绍了减压阀的主要性能,讨论了气力输送交流中减压阀的选择和调节,分析了密相气力输送系统中各种气量控制方法,对其各自的优缺点进行了详细讨论,重点分析减压阀及减压阀与拉法尔联合气量控制系统的优、缺点,表明可调式拉法尔管是今后气力输送气量控制发展的方向。     

射流管在气力输送中的应用

对物料气力输送的各种供料方式的性能、特点和使用场合进行了比较 ,重点讨论了传统文丘里供料器实际应用中存在的问题 ,介绍了几种国内外新型的文丘里供料器结构及其特点和用途。指出采用组合式供料器 ,即将文丘里供料器与机械旋转式连续供料器进行组合使用 ,可以同时改善它们两者单独使用时存在的问题。文中介绍了LAVAL管密相输送气量控制方面的应用 ,指出LAVAL管在气力输送中主要起稳定空气流量和压力的作用 ,使输送过程稳定、均匀 ,并简要介绍了气力输送系统的设计方法和步骤     

An investigation of segregation and mixing in dense phase pneumatic conveying

Pneumatic conveying of bulk materials has become an important technology in many industries: from pharmaceuticals to petro-chemicals and power generation. Particulate segregation has been investigated in many solids handling processes. However, little work has been published on the segregation and mixing in pneumatic conveying pipelines, particularly in dense phase pneumatic conveying. Due to the character of dense phase flow, it is difficult to investigate the segregation in a flowing plug. A sampling device was designed and built to take samples from the pneumatic conveying pipeline after “catching a plug”. Several experiments were conducted over a range of gas–solids flow conditions with 3 mm nylon pellets and 3 mm ballotini as a segregating mixture. Experimental data combined with video footage were analysed to describe the segregation and mixing of solids plugs in pipes. This investigation provides initial research on establishing a segregation index in a flowing plug. A gas–solids two-dimensional mathematical model was developed for plug flow of a nylon-glass particulate mixture in a horizontal pipeline in dense phase pneumatic conveying. The model was developed based on the discrete element method (DEM). The model was used to simulate the motion of particles both in a homogeneous flow and as binary mixtures taking into account the various interactions between gas, particles and pipe wall. For the gas phase, the Navier Stokes equations were integrated by the semi-implicit method for pressure-linked equations (SIMPLE) using the scheme of Patankar employing the staggered grid system. For the particle motion the Newtonian equations of motion of individual particles were integrated, where repulsive and damping forces for particle collision, the gravity force, and the drag force were taken into account. For particle contact, a model with a simple non-linear spring and dash pot model for both normal and tangential components was used. This model employed a mixture of 3 mm pellets and ballotini as virtual materials with properties of nylon and glass. The results from the model are discussed and compared with experimental work and show qualitative agreement. Further modelling and experimental work in key areas is proposed.     

An investigation of the unstable region for dense phase conveying in sliding bed flow

For fine powdered materials, capable of being conveyed in dense phase, a conveying region exists in which instability in flow and pipeline blockage can occur if the pressure gradient available is insufficient to maintain a minimum value of solids loading ratio. A reduction in material flow rate can also lead to pipeline blockage in this region. Conveying trials under-taken with cement are used to illustrate the nature of the problem.     

CHARACTERISTICS OF A HORIZONTAL SWIRLING FLOW PNEUMATIC CONVEYING WITH A CURVED PIPE

In order to prevent flow blockage phenomenon and to reduce the impact of particles on the wall of the bend, an experimental study of the swirling flow pneumatic conveying system with a horizontal curved pipe was carried out in this work. The experiment was performed in a 90-deg pipe bend with pipe diameter 75 mm and centerline curvature ratio 12. The straight pipes with 75 mm inside diameter at the upstream and downstream of the bend were 1.3 m and 4.0 m in lengths, respectively. The initial swirl number was varied from 0.22 to 0.60, the mean air velocity from 10 to 20 m/s, and the solid mass flow rate from 0.07 to 0.68 kg/s. It is found that in the lower air velocity range, the overall pressure drop of the swirling flow pneumatic conveying shows a lower tendency than that of axial flow pneumatic conveying. The minimum air velocities can be decreased by using the swirling flow pneumatic conveying. From the visualization of particle flow patterns, the impact of particles on the wall of the bend can be reduced using the swirling flow.     

CHARACTERISTICS OF A HORIZONTAL SWIRLING FLOW PNEUMATIC CONVEYING WITH A CURVED PIPE

ABSTRACT

In order to prevent flow blockage phenomenon and to reduce the impact of particles on the wall of the bend, an experimental study of the swirling flow pneumatic conveying system with a horizontal curved pipe was carried out in this work. The experiment was performed in a 90-deg pipe bend with pipe diameter 75 mm and centerline curvature ratio 12. The straight pipes with 75 mm inside diameter at the upstream and downstream of the bend were 1.3 m and 4.0 m in lengths, respectively. The initial swirl number was varied from 0.22 to 0.60, the mean air velocity from 10 to 20 m/s, and the solid mass flow rate from 0.07 to 0.68 kg/s. It is found that in the lower air velocity range, the overall pressure drop of the swirling flow pneumatic conveying shows a lower tendency than that of axial flow pneumatic conveying. The minimum air velocities can be decreased by using the swirling flow pneumatic conveying. From the visualization of particle flow patterns, the impact of particles on the wall of the bend can be reduced using the swirling flow.