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Experimental Investigation of Slugging as Initiating Water Hammer Phenomenon through Indirect Contact Steam Condensing in a Horizontal Pipe Heat Exchanger

机译:卧式管式换热器间接接触冷凝凝结引发水击现象的实验研究

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Slugging as a water hammer initiator is a fascinating topic because it has a strategic impact on equipment safety in industrial systems, i.e. pressurized water reactors (PWR), heat exchangers, etc. The present research’s objective was to investigate slugging as initiating the water hammer phenomenon through indirect contact steam condensing in a horizontal pipe heat exchanger. The experiment apparatus used in the present experimental study consisted of an inner annulus pipe made of copper (din = 17.2 mm, do = 19 mm) with a length of 1.8 m and an outer annulus pipe of galvanized iron (din = 108.3 mm, do = 114. 3 mm) with a length of 1.6 m. The tested liquid was water. The experiments were conducted at a static pressure of Ps = 108.825 kPa and the temperature of T = 119.7°C. The obtained experimental data of temperature and differential pressure fluctuations were analyzed using statistical analysis. The results were as follows: 1) the flow pattern area of non-slugging (stratified and wavy flow), transition (wavy-slug flow), and slugging (slug and large-slug) were determined, with the transition flow pattern of slug and large-slug defined as initiating water hammer; 2) transition area ranges for the wavy-slug flow pattern are from ?co=1′10-1 kg/s to ?co=6′10-1 kg/s for ?st=6′10-3 kg/s to ?st=7.5′10-3 kg/s, and ?co 3′10-1 kg/s for ?st=8′10-3 kg/s to ?st=9′10-3 kg/s. These obtained data are very important in order to develop a database for the input of an early warning system design in a safe, two-phase flow installation piping system during steam condensation.
机译:作为水锤引发剂的塞是一个引人入胜的话题,因为它对工业系统(如压水堆(PWR),换热器等)中的设备安全具有战略性影响。通过在卧式换热器中间接接触蒸汽冷凝而实现的。本实验研究中使用的实验设备由长度为1.8 m的铜制内环管(din = 17.2 mm,do = 19 mm)和镀锌铁外环管(din = 108.3 mm,do)组成。 = 114. 3 mm),长度为1.6 m。被测液体是水。实验在Ps = 108.825 kPa的静态压力和T = 119.7°C的温度下进行。使用统计分析对获得的温度和压差波动的实验数据进行分析。结果如下:1)确定了非-流(分层流和波浪流),过渡流(波浪-流)和流(sl流和大-流)的流型面积,具有流的过渡流型大块被定义为起爆水锤; 2)波浪状团状流型的过渡区域范围从?co = 1'10-1 kg / s到?co = 6'10-1 kg / s,对于?st = 6'10-3 kg / s到Δst= 7.5′10-3kg / s,Δco<3′10-1kg / s,Δst= 8′10-3kg / s至Δst= 9′10-3kg / s。这些数据对于在蒸汽凝结期间为安全的两相流安装管道系统中的预警系统设计输入数据库的开发中,非常重要。

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