污水高程水力計(jì)算表(啤酒廢水uasb工藝處理))

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1、表7-3污水高程水力計(jì)算表構(gòu)筑物名稱(chēng)構(gòu)筑物間距連接管道水力損失水面標(biāo)高流量L/s連接管徑mm流速m/s坡度‰沿程損失m局部損失m構(gòu)筑物水力損失總水力損失m上游下游構(gòu)筑物出口至計(jì)量堰8067DN2500.50.560.0450.010.05538.45538.400計(jì)量堰670.10.138.55538.455計(jì)量堰至清水池1567DN2501.3812.40.1860.1320.31838.87338.555清水池670.150.1539.02338.873清水池至氣浮池567DN2501.3812.40.0560.3830.43939.46239.023氣浮池33.

2、51.11.140.56239.462氣浮池至生物接觸氧化池233.5DN2001.0810.30.0210.0290.05040.61240.562生物接觸氧化池22.32.72.743.31240.6122生物接觸化池至UASB池2622.3DN1251.2921.20.4420.3170.75944.07143.312UASB池13.40.3680.36844.43944.071進(jìn)口0.195出口0.173UASB池至加熱池54.267DN2501.3812.40.2090.1640.37344.81244.439加熱池670.150.1544.96244.81

3、2中和池670.150.1545.11244.962調(diào)節(jié)池670.150.1545.26245.112調(diào)節(jié)池至豎流式沉淀池14.516.75DN1500.9712.50.1720.4390.61145.87345.262豎流式沉淀池3416.750.40.446.27345.873進(jìn)口0.223出口0.177豎流沉淀池至集水井6767DN2501.3812.40.4150.2060.62146.89446.2732表7-4污泥高程水力計(jì)算表構(gòu)筑物名稱(chēng)構(gòu)筑物間距連接管道水力損失總水力損失泥面標(biāo)高泥面與水面之差流量連接管徑流速坡度沿程損失局部損失構(gòu)筑物水力損失脫水間至螺桿

4、泵15288.4DN1500.180.280.00420.00760.0118螺桿泵至濃縮池288.4DN1500.180.280.002240.0050.0072濃縮池15288.41.01.039.454濃縮池至集泥池288.4DN1500.180.280.00340.00730.01072