一.一水箱连接一铅直出水管,已知:箱中水深h=1m,由于收缩影响入口A-A断面的平均流速为水管出口断面平均流速的1.5倍,设水温为20℃,相应的汽化压强为0.24N/c㎡(绝对压强),不计水头损失,试求A-A断面不发生汽化时出水管的最大长度。maxlQAmaxLhAQAmaxLhA)2/(0000)(2maxgvlh)2/(/0)2/(/22maxgvpgvplaAAgvpplAa245/)(2max)(45/)(maxlhppAahpplAa95/)(94maxm78.3maxl二.一离心式水泵,如图示,已知:Q=20m3/h,hs=5.5m,吸水管直径d=100mm,吸水管总水头损失hw=0.25m,求:(1)水泵进口处真空压强;(2)管内A点处压强水头,(吸水管底至A点处水头损失为0.20m)。Q水泵shA进口1mQ水泵shA进口1mwshgvph)2/(/0002wshgvhp)2/(/2m/s707.0/AQv78.5/pkPa6.56p(1)水泵进口处真空压强Q水泵shA进口1mAwAAhgvph12)2/(/000AwAAhgvhp12)2/(/m77.0/Ap(2)管内A点处压强水头(吸水管底至A点处水头损失为0.20m)三.一管路渐变段剖面图如图所示,已知:渐变段长度L=10m,水重G=2KN,管轴线与水平夹角,d1=200mm,d2=100mm,v1=1m/s,1-1断面表压强m水柱,不计水头损失。求:固定渐变段镇墩所受的力。3050/1pLR11vG1d1Rxz镇墩22v22dLR11vG1d1Rxz镇墩22v22ds/m03142.012.0413211vAQs/m41.041/03142.0222AQv)2/(/)2/(/22222111gvpzgvpz)]2/()2/(/)[(22211212gvgvpzzp6.19/)161(5030sin108.9kPa5.531kN39.15111ApPkN17.4222ApPLR11vG1d1Rxz镇墩22v22d)(sin1221vvQRGPPx0cosyRGkN13.10xRkN732.1yRkN277.1022yxRRR7.9/arctanxyRR四.如下图一水平射流。已知:A、v0,求时,作用在对称凸体上的力,不计摩擦力。180,90,60v0Aθ对称v0Aθ对称00cos22QvvQRx)1(cos0Qv)cos1(0QvRx180,90,600002,,21QvQvQvRx五.已知:渐变段水体重为G,p2,d1,d2,z,Δh,求:如图所示1-2渐变流段处水流对管壁的作用力,不计水头损失。G水银hd2V222Z1V11d1