某超市空调计算实例（完整）=水系统水力计算书.xls

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2440

2、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229676.7056270.001.22424.25DN500.25742.2

5、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3614875.3286500.000.81113.79

7、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435829.7533900.000.7316

8、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509676.7056270.001.22424

9、.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57811.694720.000.64407.15DN

10、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。0.1029.87315.74345.600.1032.96487.14520.101.00329.59489.79819.381.00329.59128.48458.071.00329.59142.64472.230.1031.351723.551754.901.50243.23152.55395.790.00502.6824.85527.520.1026.94139.71166.651.00269.41869.251138.671.00269.41132.64402.051.001104.5940.171144.761.50243.23152.5

14、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34522.7926

16、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109676.7

17、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249676.7056

19、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3138256.2322

20、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3729210.66169860.000.92100.65DN1001.13422.9

21、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44811.694720.000.64400.91DN201

22、.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514522.7926300.000.5797.83DN500.4016

23、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)0.15123.22121.18244.401.65681.45436.731118.181.50243.35176.35419.701.00162.23150.16312.400.00243.3539.13282.481.501163.81709.221873.041.501116.55432.671549.220.1041.90698.23740.130.1026.78644.09670.881.501113.97252.221366.201.001856.62168.152024.770.1027.43121.60149.031.00274.35402.56676.911

25、.00274.35113.11387.461.00274.35136.93411.280.1023.952177.522201.461.50243.35238.21481.560.00243.3539.13282.481.50243.35150.16393.510.00243.3539.13282.481.50243.35150.16393.510.00243.3539.13282.481.50404.3295.72500.031.00673.8663.42737.281.501113.97252.221366.201.001856.62168.152024.770.1020.22440.88

26、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。0.00243.3539.13282.480.25105.74146.21251.951.15486.40113.64600.041.1

27、5486.40433.20919.601.15486.40430.86917.250.25142.16764.39906.540.2583.951147.301231.250.2580.49548.75629.240.2550.552249.102299.651.65333.63447.52781.151.50606.60160.36766.961.501113.97260.631374.601.001856.62168.152024.771.50243.3567.81311.161.00405.5839.13444.721.50243.3567.81311.161.00405.5839.13

28、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

29、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085767.84498740.001.25112.41DN1503.93776.91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533597.59195370.001.06133.15DN100

30、4.33559.26管段629074.81169070.000.92100.86DN1009.73418.82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124522.7926300.000.5799.3

31、8DN501.53162.15管段134522.7926300.000.5799.38DN500.25162.15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195829.7533900.000.73160.6

32、8DN500.90269.41管段205829.7533900.000.73160.68DN500.25269.41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264522.7926300.000.5799.38DN

33、500.25162.15管段279676.7056270.001.22424.25DN500.81742.29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334522.7926300.000.5799.38

34、DN501.53162.15管段344522.7926300.000.5799.38DN500.25162.15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.

35、000.99116.40DN1000.04486.29管段4131329.32182180.000.99116.40DN1005.50486.29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4715011.188

36、7290.000.82115.79DN807.00335.63管段485334.4831020.000.67135.76DN502.79225.58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

37、.64407.15DN200.25202.10管段559676.7056270.001.22424.25DN500.85742.29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

38、失为45703.15 Pa。Pd(Pa)Pl(Pa)P(Pa)0.15116.54441.76558.291.50619.2059.86679.051.00412.80106.27519.071.00412.80253.54666.340.1039.77412.19451.970.1055.93575.87631.790.1041.88981.401023.280.1029.87315.74345.600.1032.96479.07512.031.00329.59494.53824.111.00329.59136.55466.141.00329.59142.64472.231.50243.23

39、152.55395.790.00502.6824.85527.520.1031.351723.551754.901.50243.23152.55395.790.00502.6824.85527.520.1026.94151.72178.661.00269.41869.251138.671.00269.41144.65414.061.001104.5940.171144.761.501113.43343.651457.071.003043.37106.063149.441.50243.2384.55327.781.00664.8324.85689.681.50243.2384.55327.781

40、.00664.8324.85689.681.501113.43343.651457.071.003043.37106.063149.441.50303.15450.49753.641.50929.67101.791031.451.501291.17299.541590.701.00860.78848.561709.331.50243.23152.55395.790.00502.6824.85527.52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。0.1068.41293.70362.111.00684.11194.02878.131.006

41、84.113238.923923.031.50404.12255.47659.590.00835.1840.17875.350.1048.635.1253.750.000.00640.45640.450.1020.21469.76489.971.50303.1581.43384.580.00626.51101.79728.301.50692.13308.801000.940.1064.702090.532155.230.1033.56810.51844.070.1022.56378.77401.331.50243.23546.81790.041.00162.15152.55314.710.00

42、502.6824.85527.521.50303.15469.76772.911.50303.1581.43384.580.00626.51101.79728.301.501113.43360.621474.041.003043.37106.063149.441.50404.12137.22541.341.001104.5940.171144.761.503109.071363.694472.761.003043.37106.063149.44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

43、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338256.23222460.001.20169.48DN1005.4

44、1725.46管段438256.23222460.001.20169.48DN1000.45725.46管段54522.7926300.000.5797.83DN501.53162.23管段64522.7926300.000.5797.83DN500.40162.23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.

45、45422.95管段1129210.66169860.000.92100.65DN1001.20422.95管段1229210.66169860.000.92100.65DN1004.35422.95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17811.694720.000.6

46、4400.91DN205.61202.20管段18811.694720.000.64400.91DN201.07202.20管段19811.694720.000.64400.91DN200.40202.20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244522.7926300.000.5797.8

47、3DN500.65162.23管段254522.7926300.000.5797.83DN500.40162.23管段269676.7056270.001.22420.37DN500.58742.65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

48、.83DN501.80162.23管段324522.7926300.000.5797.83DN501.54162.23管段334522.7926300.000.5797.83DN500.40162.23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.

49、001.22420.37DN500.63742.65管段399676.7056270.001.22420.37DN500.40742.65管段4011164.2364920.000.85153.68DN702.49364.80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

50、.000.5797.83DN501.23162.23管段464522.7926300.000.5797.83DN500.40162.23管段475829.7533900.000.73158.54DN501.59269.54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525829.7533900.000.73