冷却塔计算程序

t1t2τθPQGΔttmφraλi1i2imi1i2℃℃℃℃Kpam3/hm3/h℃℃KpaKpakg/m31433328331003300243000010383.744.980.681.120.8344.928.035.821.533.527.51.200.784324200001.12ΩnF0进塔空气焓kcal/kg出塔空气焓imt1对应的饱和焓t2对应的饱和焓tm对应的饱和焓温差平均温度Pτ汽水比Pθ相对湿度湿空气容重工况大气压力水量风量进水温度出水温度干球温度湿球温度1.55ΩHt1t2τθPQGΔttmφraλi1i2imi1i2℃℃℃℃Kpam3/hm3/h℃℃KpaKpakg/m3设计4333283399.993300243000010383.744.980.681.120.8344.928.035.821.533.527.5工况137.431.829.132.3100.9352024600005.634.63.994.790.791.140.7934.826.330.422.829.826.3工况239.232.226.136.2101.4352024200007.0135.73.345.950.451.130.7837.826.832.019.228.323.8工况339.131.126.339.199.96315025300008.0335.13.386.980.361.110.8937.825.431.219.528.524.0大气压力水量风量进水温度出水温度干球温度湿球温度tm对应的饱和焓温差平均温度Pτ汽水比Pθ相对湿度湿空气容重工况进塔空气焓kcal/kg出塔空气焓imt1对应的饱和焓t2对应的饱和焓1.200.781.551.370.741.860.840.860.981.120.821.37ΩHΩnF0