求助换热器设计问题? 大概看了看:修改 1)bhm (shell side with 2 inlet & outlet nozzle with double split flow) 2) ntiw baffle 3) shell side allowable pressure 5 kpa might be not reasonable. normally heat exchangers can use 10% of operating pressure. so i assumed to use 32 kpa allowable pressure drop for shell side. 4) tube side cooling water velocity will be lower than 1 m/s. so i increased a bit of tube side flow rate to meet tube side flow velocity 1 m/s. 5) accoustic vibration warning: shell side should install anti-resonatic baffles under shell side inlet nozzles. 6) there is no fouling resistance on shell side or tube side process data. i assumed hot air and cw fouling resistance to be 0.0002 and 0.0003. 7) tube layout: 60 degree tube layout angle is not suitable for this case. i changed into 45 degree. attached is modified htri rating. (delete ext.txt)查看更多