摘要
针对工业烟气中含尘量大,容易造成烟气换热器表面积灰的问题,对比研究了两种典型烟气余热换热器气侧的积灰特性.首先对比了两种翅片管换热器的流动特性,并结合离散相模型(DPM)模拟了飞灰颗粒的运动、碰撞和沉积过程;其次,针对模拟时间步长相对于实际时间较短的问题,提出了通过时间放大因子将数值模拟结果与时间换算到实际时间尺度的方法;然后,具体研究了实际时间尺度下两种H型翅片管表面的积灰特性,分析了入口速度和颗粒粒径的影响.结果显示,飞灰颗粒主要沉积于H型翅片管前侧的流动滞止区和管后的尾涡区;双H翅片管的积灰特性稍优于单H型翅片管;渐进污垢热阻随着入口速度和颗粒粒径的增大而迅速减小.
The problem of high exhaust temperature universally exists around the industrial boilers, which causes enormous loss of energy. Different kinds of heat exchangers are widely used in the waste heat recovery systems to recover waste energy from different heat sources. However, considering the heat exchangers mainly work in dusty environment, such as in the tail of large boiler, fly ash fouling on heat exchangers is a major problem in waste heat recovery systems, which can lead to significant efficiency deterioration. Besides, the fouling may also lead to failure of the systems with serious economic consequence. The H-type finned tube heat exchanger is a new type of heat exchanger which have been widely used in waste heat recovery systems in recent years, because of their excellent anti-wear and anti-fouling performance. In this paper, a numerical model was developed to investigate the fouling characteristics of two kinds of H-type finned tube heat exchangers used in the waste heat recovery systems. Firstly, a fouling model which contains a deposition process and a removal process is developed. The deposition process is determined by the energy balance on the particles and the removal process is determined by the the local wall shear stress and the fouling thickness on the fin surface. As the flow field directly affects the particle motion, the fluid flow characteristics of the two kinds of heat exchangers are calculated, and the discrete phase model（DPM） was employed to trace the fly ash particles in the flow field during the fouling process. Since the simulation time is much smaller in magnitude than the real time in fouling process, it is impossible to simulate the whole real fouling time period（hours） with a small time step size. In order to obtain a reliable result, it is necessary to enlarge the simulation time and results to the real time scale. In this paper, a fouling time ratio is proposed by considering the volume difference between the simulated deposit layer and the real deposited particles and
出处
《科学通报》
EI
CAS
CSCD
北大核心
2017年第12期1292-1301,共10页
Chinese Science Bulletin
基金
国家重点基础研究发展计划(2013CB228304)资助
关键词
工业余热
H型翅片管
流动特性
积灰特性
污垢热阻
industrial waste heat
H-type finned tubes
flow characteristics
fouling characteristics
fouling resistance
