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循环水量干球湿球供水温度回水温度6000333242蒸发损失水量Qe=K•△t·Q/100进塔气温,℃-1001020K,1/℃0.080.10.120.14QeK△tQ%91.80.1531060001.53风吹损失水量Qw=Pw·QQwPwQ%60.00160000.1排污损失水量Qb=(Qe/(N-1))-QwQbQeQwN%16.9591.8650.2825补水量Qm=Qe+Qw+QbQmQeQwQb%114.7591.8616.951.9125管径mm截面积m2流速m/s1500.021.80平均气温极端最高温度干球温度温度13.84333补水量100.35122.25114.75加药量计算(按干球温度计算)按7天存药量计算运行时加药量G17天加药量G2全年加药量G3单位加药量g系统容积G1=1.15*(Qw+Qb)g/1000G2=G1*24*7G3=G1*800050kg/h或L/hkg或Lt1.319625221.69710.557米顿罗隔膜泵选型型号LPH@PmaxSPMPmax(bar)Pmax(Mpa)GM00022.2536GM00054.572GM00109144GM00252572GM005050144101GM00908572GM012011572GM0170170144GM0240235144GM0330315144GM0400400144GM0500500180GB00808236GB018016772GB0250237102GB0350334144GB0450416180GB05004641440GB0600583180GB0700656102GB1000946144GB12001200180GB15001500180GB1800180020612751.20.70.51073.5310.70.350.3干球温度3040330.150.160.153初次投加量药箱总容积L300电机功率0.25KW0.25KW0.37KW(变频或恒频)0.55KW0.75KW(变频或恒频)0.75KW
本文标题:循环水补水量和加药量计算
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