污水高程水力计算表(啤酒废水uasb工艺处理))

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1、表7-3污水高程水力计算表构筑物名称构筑物间距连接管道水力损失水面标高流量L/s连接管径mm流速m/s坡度‰沿程损失m局部损失m构筑物水力损失总水力损失m上游下游构筑物出口至计量堰8067DN2500.50.560.0450.010.05538.45538.400计量堰670.10.138.55538.455计量堰至清水池1567DN2501.3812.40.1860.1320.31838.87338.555清水池670.150.1539.02338.873清水池至气浮池567DN2501.3812.40.0560.3830.43939.46239.023气浮池33.

2、51.11.140.56239.462气浮池至生物接触氧化池233.5DN2001.0810.30.0210.0290.05040.61240.562生物接触氧化池22.32.72.743.31240.6122生物接触化池至UASB池2622.3DN1251.2921.20.4420.3170.75944.07143.312UASB池13.40.3680.36844.43944.071进口0.195出口0.173UASB池至加热池54.267DN2501.3812.40.2090.1640.37344.81244.439加热池670.150.1544.96244.81

3、2中和池670.150.1545.11244.962调节池670.150.1545.26245.112调节池至竖流式沉淀池14.516.75DN1500.9712.50.1720.4390.61145.87345.262竖流式沉淀池3416.750.40.446.27345.873进口0.223出口0.177竖流沉淀池至集水井6767DN2501.3812.40.4150.2060.62146.89446.2732表7-4污泥高程水力计算表构筑物名称构筑物间距连接管道水力损失总水力损失泥面标高泥面与水面之差流量连接管径流速坡度沿程损失局部损失构筑物水力损失脱水间至螺杆

4、泵15288.4DN1500.180.280.00420.00760.0118螺杆泵至浓缩池288.4DN1500.180.280.002240.0050.0072浓缩池15288.41.01.039.454浓缩池至集泥池288.4DN1500.180.280.00340.00730.01072