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首页> 外文期刊>Aerosol Science and Technology: The Journal of the American Association for Aerosol Research >Particle Deposition in Ventilation Ducts:Connectors,Bends and Developing Turbulent Flow
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Particle Deposition in Ventilation Ducts:Connectors,Bends and Developing Turbulent Flow

机译:通风管道中的颗粒沉积:连接器,弯曲和湍流发展

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In ventilation ducts the turbulent flow profile is commonly disturbed or not fully developed,and these conditions are likely to influence particle deposition to duct surfaces.Particle deposition rates at eight S-connectors,in two 90deg duct bends and in two ducts where the turbulent flow profile was not fully developed were measured in a laboratory duct system with both bare steel and internally insulated ducts with hydraulic diameters of 15.2 cm.In the bare-steel duct system,experiments with nominal particle diameters of 1,3,5,9,and 16mum were conducted at each of three nominal air speeds:2.2,5.3,and 9.0 m/s.In the insulated duct system,deposition of particles with nominal diameters of 1,3,5,8,and 13 mum was measured at nominal air speeds of 2.2,5.3 and 8.8 m/s.Fluorescent techniques were used to measure directly the deposition velocities of monodisperse fluorescent particles to duct surfaces.Deposition at S-connectors,in bends,and in straight ducts with developing turbulence was often greater than deposition in straight ducts with fully developed turbulence for equal particle sizes,air speeds,and duct surface orientations.Deposition rates at all locations were found to increase with an increase in particle size or air speed.High deposition rates at S-connectors resulted from impaction,and these rates were nearly independent of the orientation of the S-connector.Deposition rates in the two 90° bends differed by more than an order of magnitude in some cases,probably because of the difference in turbulence conditions at the bend inlets.In straight sections of bare steel ducts where the turbulent flow profile was developing,the deposition enhancement relative to fully developed turbulence generally increased with air speed and decreased with downstream distance from the duct inlet.This enhancement was greater at the duct ceiling and wall than at the duct floor.In insulated ducts,deposition enhancement was less pronounced overall than in bare steel ducts.Trends that were observed in bare steel ducts were present,but weaker,in insulated ducts.
机译:在通风管道中,湍流分布通常受到干扰或未完全发展,这些条件可能会影响颗粒在管道表面的沉积。八个S型接头,两个90度管道弯头和两个湍流管道中的颗粒沉积速率在实验室管道系统中测量的轮廓未完全开发出来,该管道系统具有裸露的管道和水力直径为15.2 cm的内部绝缘管道。在裸露的管道系统中,标称粒径为1,3、5、9和在三种名义风速:2.2、5.3和9.0 m / s下分别进行16um的测量。在绝热管道系统中,在公称空气中测量公称直径为1,3、5、8和13mum的颗粒的沉积速度分别为2.2、5.3和8.8 m / s。使用荧光技术直接测量单分散荧光粉在管道表面的沉积速度。在S型连接器,弯头和直管中沉积湍流的现象经常发生n大于在相同粒径,风速和风管表面取向的情况下湍流充分发展的直管中的沉积量。发现所有位置的沉积率均随粒径或空气速度的增加而增加.S型连接器的高沉积率这是由于撞击造成的,并且这些速率几乎与S连接器的方向无关。在某些情况下,两个90°弯曲处的沉积速率相差一个数量级以上,可能是由于弯曲处的湍流条件不同在出现湍流分布的裸钢导管的直段中,相对于充分发展的湍流而言,沉积增强通常随风速而增加,并随着距导管入口的下游距离而减小。在导管顶部和壁处这种增强更大在隔热管道中,沉积增强总体上不如在裸钢管道中明显。趋势我们在裸露的钢管中观察到了这种现象,但在绝缘导管中却较弱。

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