[11]。（1）修正壓濾時(shí)間tt代入數(shù)據(jù)：t（2）過(guò)濾速度v①生產(chǎn)用壓濾機(jī)濾液體積VV代入數(shù)據(jù)：V②單位面積濾液體積由于實(shí)驗(yàn)裝置面積A3612.5÷400=9.03③過(guò)濾速度vv假設(shè)輔助時(shí)間tdv（3）過(guò)濾產(chǎn)率LL①截留下的干性固體質(zhì)量ww代入數(shù)據(jù)：w②過(guò)濾產(chǎn)率L代入數(shù)據(jù)：L（4）壓濾機(jī)面積AA投加10%石灰，7%鐵鹽來(lái)達(dá)成預(yù)處理。①污泥量增加系數(shù)ff②每小時(shí)污泥量每天工作兩班，每班8h，Q③壓濾機(jī)面積A代入數(shù)據(jù)：A（5）壓濾機(jī)臺(tái)數(shù)nn故此選用四臺(tái)，其中一臺(tái)備用。（6）設(shè)備選型選用型號(hào)為BM型號(hào)BM板框壓濾機(jī)主要參數(shù)及性能型號(hào)B數(shù)量（臺(tái)）4濾餅厚度（mm）30板框數(shù)（塊）35/36過(guò)濾面積（m2）40濾室容積（m3）0.605整機(jī)質(zhì)量（kg）2653地基尺寸（mm）3840整機(jī)長(zhǎng)度（mm）3794生產(chǎn)廠杭州興源過(guò)濾機(jī)有限公司4高程計(jì)算在污水處理廠高程設(shè)計(jì)計(jì)算中，高程損失分為沿程損失和局部損失。構(gòu)筑物本身產(chǎn)生的水頭損失為局部損失，污水在連接管渠中的水頭損失為沿程損失。4.1處理構(gòu)筑物的水頭損失構(gòu)筑物水頭損失構(gòu)筑物名稱水頭損失（m）中格柵及提升泵房0.3細(xì)格柵沉砂池0.2沉砂池0.3初次沉淀池0.5生化反應(yīng)池0.8電磁流量計(jì)0.1二沉池0.35機(jī)械混合池0.2旋流絮凝池0.2斜管沉淀池0.3轉(zhuǎn)盤濾池1接觸消毒池0.53.17.2各個(gè)管渠水頭損失計(jì)算（1）管線沿程損失h式中：l??管長(zhǎng)，m。（2）h式中：ξ管道局部阻力系數(shù)為：三通為1.67，彎頭為1.0，閘閥為0.06。連接管渠水力計(jì)算表管渠名稱流量Q流速v(m/s)管徑D(mm)坡度i(‰)管長(zhǎng)L(m)局部阻力系數(shù)ξ沿程損失h1(m)局部損失h2(m)合計(jì)(m)h1+h2L/sm出水口至消毒間5380.5380.859000.931500.060.0470.0020.049消毒池至轉(zhuǎn)盤濾池間5380.5380.859000.931100.060.0090.0020.012轉(zhuǎn)盤濾池間至斜管沉淀池5380.5380.859000.931213.730.0200.1370.1572690.2690.77000.903131.060.0120.0270.038斜管沉淀池至旋流絮凝池2690.2690.77000.90320.060.0020.0020.0032690.2690.77000.90320.060.0020.0020.003旋流絮凝池至機(jī)械混合池2690.2690.77000.90320.060.0020.0020.0032690.2690.77000.90320.060.0020.0020.003機(jī)械混合池至二沉池5380.5381.078001.68556.40.0920.3740.4662690.2690.77000.903551.060.0500.0270.076二沉池至配水井2690.2690.548000.47750.060.0020.0010.003配水井至反應(yīng)池5380.5381.078001.68115.54.730.1940.2760.470反應(yīng)池至初沉池2690.2690.77000.90328.32.060.0260.0520.0772690.2690.77000.90328.32.060.0260.0520.077初沉池至沉砂池5380.5381.078001.6845.58.40.0760.4910.567沉砂池至細(xì)格柵間5380.5380.859000.93153.730.0050.1370.142細(xì)格柵間至中格柵間及提升泵房5380.5380.859000.9312.