循环水平衡计算

3000900012345直流水系统循环水量R,m³/h900090009000900090001010101010R*Cp*△t/r0156.95156.95156.95156.95R*0.05%04.504.504.504.50Bt-D9000152.4573.9747.8234.74E/(K-1)9000156.9578.4752.3239.24E+Bt9000313.89235.42209.26196.18B/R%1001.690.820.530.39M/R%1003.492.622.332.1896.510.870.290.15M*C/K/100015.697.855.233.92376.67188.34125.5694.1711.305.653.772.83月投加量，t说明1.Cp为水的热容，4.187KJ/(Kg*℃）2.△t---水的进口温度与出口温度之差，℃3.r---水的蒸发潜热，2401KJ/Kg.4.此表仅为个人根据理论公式采用简化算法计算所得，与实际有所偏差，仅供参考。补充水量M,m³/h排污水量占循环水量B/R,%补充水量占循环水量M/R,%△(M/R)/△K,%阻垢剂投加量Kg/h24小时加药量Kg进出口水温差△t,℃蒸发损失水量E,m³/h风吹损失水量D,m³/h排污水量B,m³/h总排污水量Bt,m³/h循环水系统不同k值下平衡计算系统保有水量Qm³系统循环水量Rm³/h平均温差△t℃浓缩倍数，K10100678910900090009000900090001010101010156.95######156.95156.95156.954.504.504.504.504.5026.8921.6617.9215.1212.9431.3926.1622.4219.6217.44188.34######179.37176.57174.390.300.240.200.170.142.092.031.991.961.940.090.060.040.030.023.142.622.241.961.7475.3362.7853.8147.0841.852.261.881.611.411.26说明1.Cp为水的热容，4.187KJ/(Kg*℃）2.△t---水的进口温度与出口温度之差，℃3.r---水的蒸发潜热，2401KJ/Kg.4.此表仅为个人根据理论公式采用简化算法计算所得，与实际有所偏差，仅供参考。循环水系统不同k值下平衡计算药剂投加浓度ppm