5000吨天造纸中段废水处理工程设计

附表污水高程计算表序号管渠及构筑物名称Q/(l?6)管渠设计参数水头损失/m水面标高/m地面标高/mD/mmH/mi/?v(m/s)L/m工沿程局部构筑物合计上游下游构筑物上游下游1出水至二沉池295000.61.10.8100.20.011C.007一0.0180.1180.100一0.000.002二沉池29一一一一一一一一0.50.5000.6180.1180.3680.000.003二沉池至接触氧化池295000.81.80.8334.60.580.0620.020一0.0830.7000.618一0.000.004接触氧化池59一一一一一一一一0.40.4001.5141.1141.3140.000.005接触氧化池至水解酸化池594000.81.30.813.60.380.0180.012一0.0301.5441.514一0.000.006水解酸化池59一一一一一一一一0.50.5002.0441.5441.7940.000.007水解酸化池至初沉池291500.81.80.83180.380.0320.013一0.0462.0902.044一0.000.008初沉池29一一一一一一一一0.30.3002.3902.0902.2400.000.009初沉池至调节池295000.81.80.83100.60.0180.021一0.0392.4292.390一0.000.0010调节池59一一-—一一一一一0.20.2002.6292.4292.5290.000.0011调节池至格栅594000.591.21100.60.0120.031一0.0432.6722.629一0.000.0012格栅59一一一一一一一一0.10.100-2.000-2.900一0.000.0013废水至格栅59350-1.80.680.60.0140.011一0.025-2.900-2.025一0.000.00

附表二污泥高程计算表管渠及构筑物名称Q/(L?S-1)管渠设计参数水头损失/m水面标高/m地面标高/mD/mmi/%ov(m/s)L/m沿程局部构筑物合计上游下游上游下游二沉池29一一一一一一0.60.6001.0210.4210.000.00二沉池至污泥泵房292000.0040.61100.0400.005一0.0450.4210.3760.000.00提升2.95m一一一一一一一一一0.3763.3260.000.00提升泉至浓缩池6.521500.002一150.0320.004一0.0363.3263.2900.000.00浓缩池6.52一一一一一一0.50.5003.2902.7900.000.00浓缩池至贮泥池1.821500一80.0010.000一0.0022.7902.7890.000.00贮泥池1.82一一一一一一0.30.3002.7893.0910.000.00贮泥池至脱水机1.821500一120.0020.000一0.0023.0913.0890.000.00脱水机1.82一一一一一一0.50.5003.0893.5890.000.00初沉池1.82一一一一一一0.30.3002.2