1、供水管平面图水力计算书1.计算依据本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。2.计算公式a.计算摩擦阻力系数的公式采用的是柯列勃洛克怀特公式。b.管段损失 沿程损失局部损失 即：Pg Pl+Pd。c.Pdn Pd1(PmL Pz)。3.计算结果平面图水管水力计算表 编号 流量(kg/h)负荷(w)流速(m/s)Rm(Pa/m)管径 长(m)动压(Pa)管段088171.97512720.001.28118.58DN1503.93821.08管段144085.98256360.000.9176.14DN1252.68412.80管段24402、85.98256360.000.9176.14DN1254.20412.80管段335040.41203760.001.10144.38DN10021.89608.32管段430517.63177460.000.96110.68DN1001.25461.42管段530517.63177460.000.96110.68DN1001.20461.42管段630517.63177460.000.96110.68DN1004.27461.42管段730517.63177460.000.96110.68DN1001.59461.42管段820840.93121190.001.14217.31DN809.3、62646.95管段915011.1887290.000.82115.79DN807.00335.63管段105334.4831020.000.67135.76DN502.79225.58管段114522.7926300.000.5799.38DN505.52162.15管段124522.7926300.000.5799.38DN501.54162.15管段134522.7926300.000.5799.38DN500.25162.15管段14811.694720.000.64407.15DN201.13202.10管段15811.694720.000.64407.15DN200.20202.4、10管段16811.694720.000.64407.15DN200.25202.10管段179676.7056270.001.22424.25DN500.83742.29管段189676.7056270.001.22424.25DN500.25742.29管段195829.7533900.000.73160.68DN500.83269.41管段205829.7533900.000.73160.68DN500.25269.41管段219676.7056270.001.22424.25DN500.83742.29管段229676.7056270.001.22424.25DN500.25742.25、9管段234522.7926300.000.5799.38DN501.54162.15管段244522.7926300.000.5799.38DN500.25162.15管段254522.7926300.000.5799.38DN502.73162.15管段264522.7926300.000.5799.38DN500.25162.15管段274522.7926300.000.5799.38DN501.54162.15管段284522.7926300.000.5799.38DN500.25162.15管段2944085.98256360.000.9176.14DN1250.84412.80管段6、3044085.98256360.000.9176.14DN1251.35412.80管段3144085.98256360.000.9176.14DN1253.28412.80管段3243274.29251640.000.8973.47DN1255.61397.74管段3333597.59195370.001.06133.15DN1004.33559.26管段3429074.81169070.000.92100.86DN1009.73418.82管段3524552.02142770.000.7773.00DN1004.32298.66管段3614875.3286500.000.81113.797、DN804.28329.59管段3714875.3286500.000.81113.79DN804.30329.59管段3814875.3286500.000.81113.79DN801.13329.59管段3914875.3286500.000.81113.79DN801.25329.59管段4010352.5460200.000.79134.65DN7012.80313.53管段414522.7926300.000.5799.38DN501.53162.15管段424522.7926300.000.5799.38DN500.25162.15管段435829.7533900.000.73168、0.68DN500.87269.41管段445829.7533900.000.73160.68DN505.41269.41管段455829.7533900.000.73160.68DN500.83269.41管段465829.7533900.000.73160.68DN500.25269.41管段474522.7926300.000.5799.38DN501.53162.15管段484522.7926300.000.5799.38DN500.25162.15管段499676.7056270.001.22424.25DN500.85742.29管段509676.7056270.001.224249、.25DN500.25742.29管段514522.7926300.000.5799.38DN500.89162.15管段524522.7926300.000.5799.38DN500.25162.15管段534522.7926300.000.5799.38DN500.89162.15管段544522.7926300.000.5799.38DN500.25162.15管段559676.7056270.001.22424.25DN500.85742.29管段569676.7056270.001.22424.25DN500.25742.29管段57811.694720.000.64407.15DN10、201.15202.10管段58811.694720.000.64407.15DN200.25202.104.计算汇总当前最不利环路的阻力损失为43975.03 Pa。Pd(Pa)Pl(Pa)P(Pa)0.15123.16466.13589.291.65681.11204.34885.461.15474.72320.05794.762.001216.653160.874377.520.1046.14138.74184.881.00461.42132.82594.241.00461.42472.70934.121.00461.42175.98637.410.1064.702090.532155.11、230.1033.56810.51844.070.1022.56378.77401.331.50243.23549.02792.251.00162.15152.55314.710.00502.6824.85527.521.50303.15460.69763.841.50303.1581.43384.580.00626.51101.79728.301.501113.43352.131465.561.003043.37106.063149.441.50404.12133.64537.761.001104.5940.171144.761.501113.43352.131465.561.003043.12、37106.063149.441.50243.23152.55395.790.00502.6824.85527.523.15510.79271.82782.600.15527.0024.85551.853.00486.46152.55639.020.00502.6824.85527.521.50619.2063.79682.981.00412.80103.11515.901.00412.80249.61662.410.1039.77412.19451.970.1055.93575.87631.790.1041.88981.401023.28本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子13、工业部第十设计研究院主编的空气调节设计手册。0.1029.87315.74345.600.1032.96487.14520.101.00329.59489.79819.381.00329.59128.48458.071.00329.59142.64472.230.1031.351723.551754.901.50243.23152.55395.790.00502.6824.85527.520.1026.94139.71166.651.00269.41869.251138.671.00269.41132.64402.051.001104.5940.171144.761.50243.23152.514、5395.790.00502.6824.85527.521.501113.43360.621474.041.003043.37106.063149.441.50243.2388.68331.911.00664.8324.85689.681.50243.2388.68331.911.00664.8324.85689.681.501113.43360.621474.041.003043.37106.063149.441.50303.15467.43770.581.50929.67101.791031.45回水管平面图水力计算书1.计算依据本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部15、第十设计研究院主编的空气调节设计手册。2.计算公式a.计算摩擦阻力系数的公式采用的是柯列勃洛克怀特公式。b.管段损失 沿程损失局部损失 即：Pg Pl+Pd。c.Pdn Pd1(PmL Pz)。3.计算结果平面图水管水力计算表 编号 流量(kg/h)负荷(w)流速(m/s)Rm(Pa/m)管径 长(m)动压(Pa)管段088171.97512720.001.28117.57DN1501.03821.48管段144085.98256360.000.9175.30DN1255.80413.00管段24522.7926300.000.5797.83DN501.80162.23管段34522.792616、300.000.5797.83DN501.53162.23管段44522.7926300.000.5797.83DN500.40162.23管段539563.20230060.001.25180.89DN1003.92775.88管段638751.50225340.001.22173.76DN1002.49744.37管段729074.81169070.000.9299.75DN1007.00419.03管段823245.06135170.000.7364.93DN1009.92267.84管段99676.7056270.001.22420.37DN500.60742.65管段109676.717、056270.001.22420.37DN500.40742.65管段1113568.3678900.000.7494.26DN801.29274.35管段1213568.3678900.000.7494.26DN804.27274.35管段1313568.3678900.000.7494.26DN801.20274.35管段1413568.3678900.000.7494.26DN801.45274.35管段159045.5752600.000.69102.74DN7021.19239.48管段164522.7926300.000.5797.83DN502.43162.23管段174522.18、7926300.000.5797.83DN500.40162.23管段184522.7926300.000.5797.83DN501.54162.23管段194522.7926300.000.5797.83DN500.40162.23管段204522.7926300.000.5797.83DN501.54162.23管段214522.7926300.000.5797.83DN500.40162.23管段225829.7533900.000.73158.54DN500.60269.54管段235829.7533900.000.73158.54DN500.40269.54管段249676.705619、270.001.22420.37DN500.60742.65管段259676.7056270.001.22420.37DN500.40742.65管段26811.694720.000.64400.91DN201.10202.20管段27811.694720.000.64400.91DN200.20202.20管段28811.694720.000.64400.91DN200.40202.20管段2944085.98256360.000.9175.30DN1259.83413.00管段3044085.98256360.000.9175.30DN1252.79413.00管段3138256.232220、2460.001.20169.48DN1005.41725.46管段3238256.23222460.001.20169.48DN1000.37725.46管段3333733.45196160.001.06132.85DN10012.80564.07管段344522.7926300.000.5797.83DN501.53162.23管段354522.7926300.000.5797.83DN500.40162.23管段3629210.66169860.000.92100.65DN1001.45422.95管段3729210.66169860.000.92100.65DN1001.13422.921、5管段3829210.66169860.000.92100.65DN1004.30422.95管段3929210.66169860.000.92100.65DN1004.28422.95管段4019533.96113590.001.07189.91DN804.02568.63管段4115011.1887290.000.82114.39DN8010.03335.80管段4210488.3960990.000.80136.34DN704.03321.97管段43811.694720.000.64400.91DN205.61202.20管段44811.694720.000.64400.91DN20122、.12202.20管段45811.694720.000.64400.91DN200.40202.20管段469676.7056270.001.22420.37DN500.62742.65管段479676.7056270.001.22420.37DN500.40742.65管段484522.7926300.000.5797.83DN500.69162.23管段494522.7926300.000.5797.83DN500.40162.23管段504522.7926300.000.5797.83DN500.69162.23管段514522.7926300.000.5797.83DN500.401623、2.23管段529676.7056270.001.22420.37DN500.62742.65管段539676.7056270.001.22420.37DN500.40742.65管段544522.7926300.000.5797.83DN501.53162.23管段554522.7926300.000.5797.83DN500.40162.23管段565829.7533900.000.73158.54DN500.30269.54管段575829.7533900.000.73158.54DN500.40269.544.计算汇总当前最不利环路的阻力损失为14913.14 Pa。Pd(Pa)Pl(24、Pa)P(Pa)0.15123.22121.18244.401.65681.45436.731118.181.50243.35176.35419.701.00162.23150.16312.400.00243.3539.13282.481.501163.81709.221873.041.501116.55432.671549.220.1041.90698.23740.130.1026.78644.09670.881.501113.97252.221366.201.001856.62168.152024.770.1027.43121.60149.031.00274.35402.56676.91125、.00274.35113.11387.461.00274.35136.93411.280.1023.952177.522201.461.50243.35238.21481.560.00243.3539.13282.481.50243.35150.16393.510.00243.3539.13282.481.50243.35150.16393.510.00243.3539.13282.481.50404.3295.72500.031.00673.8663.42737.281.501113.97252.221366.201.001856.62168.152024.770.1020.22440.8826、461.101.50303.3080.18383.480.00303.30160.36463.660.25103.25739.96843.211.15474.95210.08685.030.25181.37916.901098.271.15834.2862.76897.040.25141.021700.541841.561.50243.35150.16393.51本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。0.00243.3539.13282.480.25105.74146.21251.951.15486.40113.64600.041.127、5486.40433.20919.601.15486.40430.86917.250.25142.16764.39906.540.2583.951147.301231.250.2580.49548.75629.240.2550.552249.102299.651.65333.63447.52781.151.50606.60160.36766.961.501113.97260.631374.601.001856.62168.152024.771.50243.3567.81311.161.00405.5839.13444.721.50243.3567.81311.161.00405.5839.1328、444.721.501113.97260.631374.601.001856.62168.152024.771.50243.35150.16393.510.00243.3539.13282.481.50404.3247.17451.481.00673.8663.42737.28供水管平面图水力计算书1.计算依据2.计算公式a.计算摩擦阻力系数的公式采用的是柯列勃洛克怀特公式。b.管段损失 沿程损失局部损失 即：Pg Pl+Pd。c.Pdn Pd1(PmL Pz)。3.计算结果平面图水管水力计算表 编号 流量(kg/h)负荷(w)流速(m/s)Rm(Pa/m)管径 长(m)动压(Pa)管段08529、767.84498740.001.25112.41DN1503.93776.91管段144085.98256360.000.9176.14DN1250.79412.80管段244085.98256360.000.9176.14DN1251.40412.80管段344085.98256360.000.9176.14DN1253.33412.80管段443274.29251640.000.8973.47DN1255.61397.74管段533597.59195370.001.06133.15DN1004.33559.26管段629074.81169070.000.92100.86DN1009.7330、418.82管段724552.02142770.000.7773.00DN1004.32298.66管段814875.3286500.000.81113.79DN804.21329.59管段914875.3286500.000.81113.79DN804.35329.59管段1014875.3286500.000.81113.79DN801.20329.59管段1114875.3286500.000.81113.79DN801.25329.59管段124522.7926300.000.5799.38DN501.53162.15管段134522.7926300.000.5799.38DN500.31、25162.15管段1410352.5460200.000.79134.65DN7012.80313.53管段154522.7926300.000.5799.38DN501.53162.15管段164522.7926300.000.5799.38DN500.25162.15管段175829.7533900.000.73160.68DN500.94269.41管段185829.7533900.000.73160.68DN505.41269.41管段195829.7533900.000.73160.68DN500.90269.41管段205829.7533900.000.73160.68DN50032、.25269.41管段219676.7056270.001.22424.25DN500.81742.29管段229676.7056270.001.22424.25DN500.25742.29管段234522.7926300.000.5799.38DN500.85162.15管段244522.7926300.000.5799.38DN500.25162.15管段254522.7926300.000.5799.38DN500.85162.15管段264522.7926300.000.5799.38DN500.25162.15管段279676.7056270.001.22424.25DN500.8133、742.29管段289676.7056270.001.22424.25DN500.25742.29管段29811.694720.000.64407.15DN201.11202.10管段30811.694720.000.64407.15DN200.25202.10管段3141681.86242380.001.31201.87DN1001.48860.78管段3241681.86242380.001.31201.87DN1004.20860.78管段334522.7926300.000.5799.38DN501.53162.15管段344522.7926300.000.5799.38DN500.234、5162.15管段3537159.07216080.001.17161.68DN1001.82684.11管段3637159.07216080.001.17161.68DN1001.20684.11管段3737159.07216080.001.17161.68DN10020.03684.11管段385829.7533900.000.73160.68DN501.59269.41管段395829.7533900.000.73160.68DN500.25269.41管段4031329.32182180.000.99116.40DN1000.04486.29管段4131329.32182180.00035、.99116.40DN1005.50486.29管段42811.694720.000.64407.15DN201.15202.10管段43811.694720.000.64407.15DN200.20202.10管段44811.694720.000.64407.15DN200.25202.10管段4530517.63177460.000.96110.68DN1002.79461.42管段4620840.93121190.001.14217.31DN809.62646.95管段4715011.1887290.000.82115.79DN807.00335.63管段485334.4831020.036、00.67135.76DN502.79225.58管段494522.7926300.000.5799.38DN505.50162.15管段504522.7926300.000.5799.38DN501.54162.15管段514522.7926300.000.5799.38DN500.25162.15管段52811.694720.000.64407.15DN201.15202.10管段53811.694720.000.64407.15DN200.20202.10管段54811.694720.000.64407.15DN200.25202.10管段559676.7056270.001.2242437、.25DN500.85742.29管段569676.7056270.001.22424.25DN500.25742.29管段575829.7533900.000.73160.68DN500.85269.41管段585829.7533900.000.73160.68DN500.25269.41管段599676.7056270.002.041604.34DN400.852072.71管段609676.7056270.001.22424.25DN500.25742.294.计算汇总当前最不利环路的阻力损失为45703.15 Pa。Pd(Pa)Pl(Pa)P(Pa)0.15116.54441.765538、8.291.50619.2059.86679.051.00412.80106.27519.071.00412.80253.54666.340.1039.77412.19451.970.1055.93575.87631.790.1041.88981.401023.280.1029.87315.74345.600.1032.96479.07512.031.00329.59494.53824.111.00329.59136.55466.141.00329.59142.64472.231.50243.23152.55395.790.00502.6824.85527.520.1031.351723.5539、1754.901.50243.23152.55395.790.00502.6824.85527.520.1026.94151.72178.661.00269.41869.251138.671.00269.41144.65414.061.001104.5940.171144.761.501113.43343.651457.071.003043.37106.063149.441.50243.2384.55327.781.00664.8324.85689.681.50243.2384.55327.781.00664.8324.85689.681.501113.43343.651457.071.00340、043.37106.063149.441.50303.15450.49753.641.50929.67101.791031.451.501291.17299.541590.701.00860.78848.561709.331.50243.23152.55395.790.00502.6824.85527.520.1068.41293.70362.111.00684.11194.02878.131.00684.113238.923923.031.50404.12255.47659.590.00835.1840.17875.350.1048.635.1253.750.000.00640.45640.41、450.1020.21469.76489.971.50303.1581.43384.580.00626.51101.79728.301.50692.13308.801000.940.1064.702090.532155.230.1033.56810.51844.070.1022.56378.77401.331.50243.23546.81790.041.00162.15152.55314.710.00502.6824.85527.521.50303.15469.76772.911.50303.1581.43384.580.00626.51101.79728.301.501113.43360.642、21474.041.003043.37106.063149.441.50404.12137.22541.341.001104.5940.171144.761.503109.071363.694472.761.003043.37106.063149.44回水管平面图水力计算书1.计算依据本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。2.计算公式a.计算摩擦阻力系数的公式采用的是柯列勃洛克怀特公式。b.管段损失 沿程损失局部损失 即：Pg Pl+Pd。c.Pdn Pd1(PmL Pz)。3.计算结果平面图水管水力计算表 编号 流量(kg/h)负荷43、(w)流速(m/s)Rm(Pa/m)管径 长(m)动压(Pa)管段085767.84498740.001.25111.43DN1501.03777.29管段144085.98256360.000.9175.30DN1259.75413.00管段244085.98256360.000.9175.30DN1252.81413.00管段338256.23222460.001.20169.48DN1005.41725.46管段438256.23222460.001.20169.48DN1000.45725.46管段54522.7926300.000.5797.83DN501.53162.23管段64544、22.7926300.000.5797.83DN500.40162.23管段733733.45196160.001.06132.85DN10012.80564.07管段84522.7926300.000.5797.83DN501.53162.23管段94522.7926300.000.5797.83DN500.40162.23管段1029210.66169860.000.92100.65DN1001.45422.95管段1129210.66169860.000.92100.65DN1001.20422.95管段1229210.66169860.000.92100.65DN1004.35422.45、95管段1329210.66169860.000.92100.65DN1004.21422.95管段1419533.96113590.001.07189.91DN804.02568.63管段1515011.1887290.000.82114.39DN8010.03335.80管段1610488.3960990.000.80136.34DN704.03321.97管段17811.694720.000.64400.91DN205.61202.20管段18811.694720.000.64400.91DN201.07202.20管段19811.694720.000.64400.91DN200.40246、02.20管段209676.7056270.001.22420.37DN500.58742.65管段219676.7056270.001.22420.37DN500.40742.65管段224522.7926300.000.5797.83DN500.65162.23管段234522.7926300.000.5797.83DN500.40162.23管段244522.7926300.000.5797.83DN500.65162.23管段254522.7926300.000.5797.83DN500.40162.23管段269676.7056270.001.22420.37DN500.58742.47、65管段279676.7056270.001.22420.37DN500.40742.65管段285829.7533900.000.73158.54DN500.37269.54管段295829.7533900.000.73158.54DN500.40269.54管段3041681.86242380.001.31200.17DN1005.78861.20管段314522.7926300.000.5797.83DN501.80162.23管段324522.7926300.000.5797.83DN501.54162.23管段334522.7926300.000.5797.83DN500.4016248、.23管段3437159.07216080.001.17160.19DN1003.90684.45管段3536347.38211360.001.14153.48DN1002.49654.87管段3626670.68155090.000.8484.50DN1007.00352.60管段3720840.93121190.001.14215.24DN809.92647.27管段389676.7056270.001.22420.37DN500.63742.65管段399676.7056270.001.22420.37DN500.40742.65管段4011164.2364920.000.85153.649、8DN702.49364.80管段4110352.5460200.000.79132.97DN705.77313.68管段424522.7926300.000.5797.83DN5019.50162.23管段434522.7926300.000.5797.83DN501.20162.23管段444522.7926300.000.5797.83DN501.62162.23管段454522.7926300.000.5797.83DN501.23162.23管段464522.7926300.000.5797.83DN500.40162.23管段475829.7533900.000.73158.54D50、N501.59269.54管段485829.7533900.000.73158.54DN500.40269.54管段49811.694720.000.64400.91DN201.12202.20管段50811.694720.000.64400.91DN200.20202.20管段51811.694720.000.64400.91DN200.40202.20管段525829.7533900.000.73158.54DN500.63269.54管段535829.7533900.000.73158.54DN500.40269.54管段549676.7056270.001.22420.37DN500.51、63742.65管段559676.7056270.001.22420.37DN500.40742.65管段56811.694720.000.64400.91DN201.12202.20管段57811.694720.000.64400.91DN200.20202.20管段58811.694720.000.64400.91DN200.40202.204.计算汇总当前最不利环路的阻力损失为13972.00 Pa。Pd(Pa)Pl(Pa)P(Pa)0.15116.59114.77231.370.1041.30734.33775.631.00413.00211.97624.970.1072.55916.52、90989.451.00725.4675.43800.891.50243.35150.16393.510.00243.3539.13282.480.1056.411700.541756.941.50243.35150.16393.510.00243.3539.13282.480.1042.30146.21188.501.00422.95120.78543.731.00422.95437.39860.341.00422.95423.72846.670.1056.86764.39821.250.1033.581147.301180.880.1032.20548.75580.950.1020.22253、249.102269.321.50303.30430.84734.141.50606.60160.36766.961.501113.97243.821357.791.001856.62168.152024.771.50243.3563.74307.091.00405.5839.13444.721.50243.3563.74307.091.00405.5839.13444.721.501113.97243.821357.791.001856.62168.152024.771.50404.3259.02463.331.00673.8663.42737.281.701464.041155.9626154、9.991.50243.35176.35419.701.00162.23150.16312.400.00243.3539.13282.481.501026.67624.501651.17本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。1.50982.31382.181364.480.1035.26591.48626.740.1064.732135.212199.941.501113.97264.831378.811.001856.62168.152024.770.1036.48382.67419.151.50470.52767.781238.355、12.00324.471908.062232.531.00162.23117.39279.631.00162.23158.22320.451.00162.23120.82283.050.00243.3539.13282.483.00808.63252.081060.710.00404.3263.42467.731.50303.30449.81753.111.50303.3080.18383.480.00303.30160.36463.661.50404.3299.25503.571.00673.8663.42737.281.501113.97264.831378.811.001856.621656、8.152024.770.1020.22449.81470.031.50303.3080.18383.480.00303.30160.36463.66供水管平面图水力计算书1.计算依据本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。2.计算公式a.计算摩擦阻力系数的公式采用的是柯列勃洛克怀特公式。b.管段损失 沿程损失局部损失 即：Pg Pl+Pd。c.Pdn Pd1(PmL Pz)。3.计算结果平面图水管水力计算表 编号 流量(kg/h)负荷(w)流速(m/s)Rm(Pa/m)管径 长(m)动压(Pa)管段018663.80108530.0057、1.02175.73DN801.08518.84管段19647.4656100.000.74117.73DN7030.70272.28管段29647.4656100.000.74117.73DN7026.38272.28管段39647.4656100.000.74117.73DN702.50272.28管段41262.257340.000.61275.75DN251.82187.52管段5631.133670.000.49253.91DN201.19122.18管段6631.133670.000.49253.91DN200.25122.18管段7631.133670.000.49253.91D58、N200.28122.18管段8631.133670.000.49253.91DN200.25122.18管段98385.2148760.000.6490.22DN704.36205.69管段10631.133670.000.49253.91DN201.78122.18管段11631.133670.000.49253.91DN200.25122.18管段127754.0845090.000.5977.81DN702.04175.89管段137754.0845090.000.5977.81DN702.36175.89管段143786.7622020.000.80262.13DN402.8731759、.41管段153155.6318350.000.66185.42DN403.96220.42管段161893.3811010.000.52142.00DN326.34137.27管段17631.133670.000.49253.91DN205.40122.18管段18631.133670.000.49253.91DN202.40122.18管段19631.133670.000.49253.91DN200.25122.18管段201262.257340.000.61275.75DN252.40187.52管段21631.133670.000.49253.91DN200.85122.18管段22660、31.133670.000.49253.91DN200.25122.18管段23631.133670.000.49253.91DN200.67122.18管段24631.133670.000.49253.91DN200.25122.18管段251262.257340.000.61275.75DN252.40187.52管段26631.133670.000.49253.91DN200.61122.18管段27631.133670.000.49253.91DN200.25122.18管段28631.133670.000.49253.91DN200.91122.18管段29631.133670.0061、0.49253.91DN200.25122.18管段30631.133670.000.49253.91DN202.40122.18管段31631.133670.000.49253.91DN200.25122.18管段323967.3323070.000.83286.47DN402.40348.40管段333155.6318350.000.66185.42DN404.99220.42管段343155.6318350.000.66185.42DN405.89220.42管段353155.6318350.000.66185.42DN401.14220.42管段36631.133670.000.49262、53.91DN200.63122.18管段37631.133670.000.49253.91DN200.25122.18管段382524.5114680.000.70244.28DN322.86244.04管段392524.5114680.000.70244.28DN320.52244.04管段40631.133670.000.49253.91DN200.63122.18管段41631.133670.000.49253.91DN200.25122.18管段421893.3811010.000.52142.00DN323.07137.27管段431262.257340.000.61275.75D63、N250.61187.52管段441262.257340.000.61275.75DN252.70187.52管段45631.133670.000.49253.91DN201.70122.18管段46631.133670.000.49253.91DN201.58122.18管段47631.133670.000.49253.91DN200.58122.18管段48631.133670.000.49253.91DN200.25122.18管段49631.133670.000.49253.91DN200.50122.18管段50631.133670.000.49253.91DN200.25122.164、8管段51631.133670.000.49253.91DN200.61122.18管段52631.133670.000.49253.91DN200.25122.18管段53811.694720.000.64407.15DN200.37202.10管段54811.694720.000.64407.15DN200.25202.10管段559016.3452430.000.69103.52DN700.30237.82管段569016.3452430.000.69103.52DN7010.06237.82管段578385.2148760.000.6490.22DN705.58205.69管段587165、22.9641420.000.90235.44DN506.45402.20管段595860.7134080.000.74162.30DN506.15272.28管段605049.0129360.000.64122.33DN502.75202.08管段61631.133670.000.49253.91DN203.29122.18管段62631.133670.000.49253.91DN202.10122.18管段63631.133670.000.49253.91DN200.25122.18管段644417.8825690.000.93351.85DN402.85432.03管段653155.6366、18350.000.66185.42DN406.94220.42管段661893.3811010.000.52142.00DN326.98137.27管段67631.133670.000.49253.91DN206.12122.18管段68631.133670.000.49253.91DN202.10122.18管段69631.133670.000.49253.91DN200.25122.18管段701262.257340.000.61275.75DN252.10187.52管段71631.133670.000.49253.91DN200.94122.18管段72631.133670.000.67、49253.91DN200.25122.18管段73631.133670.000.49253.91DN200.88122.18管段74631.133670.000.49253.91DN200.25122.18管段751262.257340.000.61275.75DN252.10187.52管段76631.133670.000.49253.91DN200.92122.18管段77631.133670.000.49253.91DN200.25122.18管段78631.133670.000.49253.91DN200.90122.18管段79631.133670.000.49253.91DN2068、0.25122.18管段801262.257340.000.61275.75DN252.10187.52管段81631.133670.000.49253.91DN200.86122.18管段82631.133670.000.49253.91DN200.25122.18管段83631.133670.000.49253.91DN200.96122.18管段84631.133670.000.49253.91DN200.25122.18管段85811.694720.000.64407.15DN202.10202.10管段86811.694720.000.64407.15DN200.25202.10管段69、871262.257340.000.61275.75DN252.10187.52管段88631.133670.000.49253.91DN200.76122.18管段89631.133670.000.49253.91DN200.25122.18管段90631.133670.000.49253.91DN200.76122.18管段91631.133670.000.49253.91DN200.25122.18管段921262.257340.000.61275.75DN252.10187.52管段93631.133670.000.49253.91DN200.70122.18管段94631.1336770、0.000.49253.91DN200.25122.18管段95631.133670.000.49253.91DN200.82122.18管段96631.133670.000.49253.91DN200.25122.18管段97631.133670.000.49253.91DN202.10122.18管段98631.133670.000.49253.91DN200.25122.184.计算汇总当前最不利环路的阻力损失为43727.24 Pa。Pd(Pa)Pl(Pa)P(Pa)0.1577.83189.79267.621.50408.423613.704022.121.00272.283105.71、553377.831.00272.28294.66566.941.50281.29500.62781.911.50183.28303.11486.380.00378.7763.48442.251.50183.2871.40254.680.00378.7763.48442.250.1020.57393.57414.141.50183.28452.56635.831.50562.0563.48625.530.1017.59159.01176.601.00175.89183.61359.500.1031.74751.69783.430.1022.04733.66755.710.1013.73900.72、63914.360.1012.221371.351383.561.50183.28608.82792.101.50562.0563.48625.531.50281.29661.18942.471.50183.28215.24398.520.00378.7763.48442.251.50183.28170.71353.990.00378.7763.48442.251.50281.29661.18942.471.50183.28156.07339.350.00378.7763.48442.251.50183.28229.88413.150.00378.7763.48442.251.50183.2873、608.82792.101.50562.0563.48625.531.50522.60686.881209.480.1022.04926.06948.101.00220.421092.791313.21本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。1.00220.42210.98431.401.50183.28160.68343.961.50562.0563.48625.530.1024.40698.69723.101.00244.04127.82371.871.50183.28160.59343.861.50562.0563.48625.574、30.1013.73436.41450.140.1018.75168.71187.461.50281.29743.311024.600.1012.22431.89444.111.50183.28400.44583.711.50183.28146.51329.791.50562.0563.48625.531.50183.28127.06310.341.50562.0563.48625.531.50183.28155.95339.221.50562.0563.48625.531.50303.15151.00454.150.00626.51101.79728.300.1023.7831.0654.875、41.00237.821041.021278.830.1020.57503.68524.250.1040.221519.761559.970.1027.23998.511025.740.1020.21336.42356.631.50183.28835.381018.661.50183.28532.65715.931.50562.0563.48625.531.50648.041001.401649.440.1022.041287.361309.400.1013.73991.541005.270.1012.221553.541565.751.50183.28532.65715.931.50562.76、0563.48625.531.50281.29578.46859.741.50183.28238.26421.540.00378.7763.48442.251.50183.28223.86407.140.00378.7763.48442.251.50281.29578.46859.741.50183.28233.82417.100.00378.7763.48442.251.50183.28228.30411.580.00378.7763.48442.251.50281.29578.46859.741.50183.28219.36402.640.00378.7763.48442.251.501877、3.28242.76426.040.00378.7763.48442.251.50303.15854.091157.241.50929.67101.791031.451.50281.29578.46859.741.50183.28193.54376.820.00378.7763.48442.251.50183.28192.41375.690.00378.7763.48442.251.50281.29578.46859.741.50183.28178.47361.740.00378.7763.48442.251.50183.28207.48390.760.00378.7763.48442.25178、.50183.28532.65715.931.50562.0563.48625.53回水管平面图水力计算书1.计算依据本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。2.计算公式a.计算摩擦阻力系数的公式采用的是柯列勃洛克怀特公式。b.管段损失 沿程损失局部损失 即：Pg Pl+Pd。c.Pdn Pd1(PmL Pz)。3.计算结果平面图水管水力计算表 编号 流量(kg/h)负荷(w)流速(m/s)Rm(Pa/m)管径 长(m)动压(Pa)管段018663.80108530.001.02173.92DN801.48519.10管段19016.379、452430.000.69102.11DN703.51237.93管段28385.2148760.000.6488.92DN706.42205.79管段37122.9641420.000.90232.72DN506.98402.39管段45860.7134080.000.74160.15DN506.94272.41管段51262.257340.000.61271.47DN252.43187.62管段6631.133670.000.49249.34DN200.86122.24管段7631.133670.000.49249.34DN200.40122.24管段8631.133670.000.49280、49.34DN200.66122.24管段9631.133670.000.49249.34DN200.40122.24管段104598.4526740.000.58100.95DN502.55167.71管段113967.3323070.000.84282.95DN402.45348.57管段123155.6318350.000.66182.75DN406.45220.53管段131893.3811010.000.52139.61DN326.45137.34管段14631.133670.000.49249.34DN205.58122.24管段15631.133670.000.49249.34D81、N202.43122.24管段16631.133670.000.49249.34DN200.40122.24管段171262.257340.000.61271.47DN252.43187.62管段18631.133670.000.49249.34DN200.40122.24管段19631.133670.000.49249.34DN200.40122.24管段20631.133670.000.49249.34DN200.82122.24管段21631.133670.000.49249.34DN200.40122.24管段221262.257340.000.61271.47DN252.43187.82、62管段23631.133670.000.49249.34DN200.76122.24管段24631.133670.000.49249.34DN200.40122.24管段25631.133670.000.49249.34DN200.46122.24管段26631.133670.000.49249.34DN200.40122.24管段27811.694720.000.64400.91DN202.43202.20管段28811.694720.000.64400.91DN200.40202.20管段29631.133670.000.49249.34DN203.59122.24管段30631.13383、670.000.49249.34DN202.43122.24管段31631.133670.000.49249.34DN200.40122.24管段321262.257340.000.61271.47DN252.43187.62管段33631.133670.000.49249.34DN200.60122.24管段34631.133670.000.49249.34DN200.40122.24管段35631.133670.000.49249.34DN200.92122.24管段36631.133670.000.49249.34DN200.40122.24管段371262.257340.000.61284、71.47DN252.43187.62管段38631.133670.000.49249.34DN200.94122.24管段39631.133670.000.49249.34DN200.40122.24管段40631.133670.000.49249.34DN200.58122.24管段41631.133670.000.49249.34DN200.40122.24管段42631.133670.000.49249.34DN202.43122.24管段43631.133670.000.49249.34DN200.40122.24管段449647.4656100.000.74116.19DN700.85、19272.41管段459647.4656100.000.74116.19DN702.71272.41管段461262.257340.000.61271.47DN251.85187.62管段47631.133670.000.49249.34DN200.89122.24管段48631.133670.000.49249.34DN200.40122.24管段49631.133670.000.49249.34DN200.28122.24管段50631.133670.000.49249.34DN200.40122.24管段518385.2148760.000.6488.92DN704.06205.79管86、段52631.133670.000.49249.34DN201.82122.24管段53631.133670.000.49249.34DN200.40122.24管段547754.0845090.000.5976.64DN702.26175.98管段557754.0845090.000.5976.64DN702.58175.98管段563786.7622020.000.80258.80DN402.87317.56管段573155.6318350.000.66182.75DN403.96220.53管段581893.3811010.000.52139.61DN326.34137.34管段596387、1.133670.000.49249.34DN205.40122.24管段60631.133670.000.49249.34DN202.43122.24管段61631.133670.000.49249.34DN200.40122.24管段621262.257340.000.61271.47DN252.43187.62管段63631.133670.000.49249.34DN200.85122.24管段64631.133670.000.49249.34DN200.40122.24管段65631.133670.000.49249.34DN200.37122.24管段66631.133670.00088、.49249.34DN200.40122.24管段671262.257340.000.61271.47DN252.43187.62管段68631.133670.000.49249.34DN200.91122.24管段69631.133670.000.49249.34DN200.40122.24管段70631.133670.000.49249.34DN200.31122.24管段71631.133670.000.49249.34DN200.40122.24管段72631.133670.000.49249.34DN202.43122.24管段73631.133670.000.49249.34DN289、00.40122.24管段743967.3323070.000.84282.95DN402.43348.57管段753155.6318350.000.66182.75DN404.96220.53管段763155.6318350.000.66182.75DN406.08220.53管段773155.6318350.000.66182.75DN401.35220.53管段782524.5114680.000.70240.86DN322.71244.16管段792524.5114680.000.70240.86DN320.73244.16管段80631.133670.000.49249.34DN2090、0.93122.24管段81631.133670.000.49249.34DN200.40122.24管段821893.3811010.000.52139.61DN323.03137.34管段831262.257340.000.61271.47DN250.50187.62管段841262.257340.000.61271.47DN252.88187.62管段85631.133670.000.49249.34DN201.57122.24管段86631.133670.000.49249.34DN201.76122.24管段87631.133670.000.49249.34DN200.90122.291、4管段88631.133670.000.49249.34DN200.40122.24管段89631.133670.000.49249.34DN200.83122.24管段90631.133670.000.49249.34DN200.40122.24管段91631.133670.000.49249.34DN200.95122.24管段92631.133670.000.49249.34DN200.40122.24管段93631.133670.000.49249.34DN200.94122.24管段94631.133670.000.49249.34DN200.40122.24管段95811.694792、20.000.64400.91DN200.37202.20管段96811.694720.000.64400.91DN200.40202.204.计算汇总当前最不利环路的阻力损失为11198.00 Pa。Pd(Pa)Pl(Pa)P(Pa)0.000.00257.51257.511.50356.90358.02714.920.1020.58570.75591.320.1040.241625.001665.240.1027.241111.951139.191.50281.42659.56940.991.50183.37215.41398.780.00183.3799.74283.101.50183.93、37163.59346.950.00183.3799.74283.100.1016.77257.03273.801.50522.86693.231216.080.1022.051179.141201.200.1013.73901.16914.900.1012.221392.021404.241.50183.37605.78789.151.50366.7399.74466.471.50281.42659.56940.991.50183.37100.45283.820.00183.3799.74283.101.50183.37203.74387.110.00183.3799.74283.101.594、0281.42659.56940.991.50183.37190.05373.420.00183.3799.74283.101.50183.37114.14297.510.00183.3799.74283.101.50303.30974.031277.331.50606.60160.36766.960.1012.22895.12907.351.50183.37605.78789.151.50366.7399.74466.471.50281.42659.56940.991.50183.37149.38332.750.00183.3799.74283.10本计算方法理论依据是陆耀庆编著的供暖通风设95、计手册和电子工业部第十设计研究院主编的空气调节设计手册。1.50183.37229.61412.980.00183.3799.74283.101.50281.42659.56940.991.50183.37233.97417.330.00183.3799.74283.101.50183.37145.03328.400.00183.3799.74283.101.50183.37605.78789.151.50366.7399.74466.471.50408.6222.15430.771.00272.41315.06587.473.00562.85501.181064.031.50183.372296、2.84406.210.00183.3799.74283.101.50183.3770.11253.480.00183.3799.74283.102.00411.58361.26772.851.50183.37452.61635.981.50366.7399.74466.470.1017.60173.12190.721.00175.98197.45373.430.1031.76742.14773.900.1022.05723.11745.160.1013.73885.45899.180.1012.221346.631358.851.50183.37605.78789.151.50366.73997、9.74466.471.50281.42659.56940.991.50183.37211.36394.730.00183.3799.74283.101.50183.3792.83276.200.00183.3799.74283.101.50281.42659.56940.991.50183.37225.73409.100.00183.3799.74283.101.50183.3778.46261.830.00183.3799.74283.101.50183.37605.78789.151.50366.7399.74466.471.50522.86687.441210.300.1022.05998、06.93928.981.00220.531110.301330.831.00220.53246.04466.570.1024.42651.97676.391.00244.16175.82419.991.50183.37231.98415.341.50366.7399.74466.470.1013.73422.84436.570.1018.76135.40154.161.50281.42780.531061.960.1012.22391.19403.411.50183.37438.06621.431.50183.37224.84408.211.50366.7399.74466.471.501899、3.37206.73390.091.50366.7399.74466.471.50183.37238.00421.371.50366.7399.74466.471.50183.37234.11417.481.50366.7399.74466.471.50303.30148.68451.980.00303.30160.36463.66水管立管水力计算书1.计算依据本计算方法理论依据是陆耀庆编著的供暖通风设计手册和电子工业部第十设计研究院主编的空气调节设计手册。2.计算公式a.计算摩擦阻力系数的公式采用的是柯列勃洛克怀特公式。b.管段损失 沿程损失局部损失 即：Pg Pl+Pd。c.Pdn Pd1100、(PmL Pz)。3.计算结果（异程系统）供水立管水力计算表编号流量(kg/h)负荷(w)流速(m/s)管径Rm(Pa/m)长(m)动压(Pa)1192603.6111199901.45DN20099.3931046.4322173939.8110114601.31DN20081.573853.451388171.975127201.28DN150118.582.6821.081小计454715.3926441708.62720.96回水立管水力计算表编号流量(kg/h)负荷(w)流速(m/s)管径Rm(Pa/m)长(m)动压(Pa)1192603.6111199901.45DN20099.3101、931046.4322173939.8110114601.31DN20081.573853.451388171.975127201.28DN150118.582.6821.081小计454715.3926441708.62720.96Pd(Pa)Pl(Pa)P(Pa)2092.86298.162391.02853.45244.71098.15821.08308.311129.393767.39851.174618.56Pd(Pa)Pl(Pa)P(Pa)2092.86298.162391.02853.45244.71098.15821.08308.311129.393767.39851.174618.56