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1、供水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水力計(jì)算表 編號(hào) 流量(kg/h) 負(fù)荷(w) 流速(m/s)Rm(Pa/m)管徑 長(zhǎng)(m)動(dòng)壓(Pa) 管段088171.97512720.001.28118.58DN1503.93821.080.15管段144085.98256360.000.9176.14DN1252.6841
2、2.801.65管段244085.98256360.000.9176.14DN1254.20412.801.15管段335040.41203760.001.10144.38DN10021.89608.322.00管段430517.63177460.000.96110.68DN1001.25461.420.10管段530517.63177460.000.96110.68DN1001.20461.421.00管段630517.63177460.000.96110.68DN1004.27461.421.00管段730517.63177460.000.96110.68DN1001.59461.421.
3、00管段820840.93121190.001.14217.31DN809.62646.950.10管段915011.1887290.000.82115.79DN807.00335.630.10管段105334.4831020.000.67135.76DN502.79225.580.10管段114522.7926300.000.5799.38DN505.52162.151.50管段124522.7926300.000.5799.38DN501.54162.151.00管段134522.7926300.000.5799.38DN500.25162.150.00管段14811.694720.000
4、.64407.15DN201.13202.101.50管段15811.694720.000.64407.15DN200.20202.101.50管段16811.694720.000.64407.15DN200.25202.100.00管段179676.7056270.001.22424.25DN500.83742.291.50管段189676.7056270.001.22424.25DN500.25742.291.00管段195829.7533900.000.73160.68DN500.83269.411.50管段205829.7533900.000.73160.68DN500.25269.4
5、11.00管段219676.7056270.001.22424.25DN500.83742.291.50管段229676.7056270.001.22424.25DN500.25742.291.00管段234522.7926300.000.5799.38DN501.54162.151.50管段244522.7926300.000.5799.38DN500.25162.150.00管段254522.7926300.000.5799.38DN502.73162.153.15管段264522.7926300.000.5799.38DN500.25162.150.15管段274522.7926300.
6、000.5799.38DN501.54162.153.00管段284522.7926300.000.5799.38DN500.25162.150.00管段2944085.98256360.000.9176.14DN1250.84412.801.50管段3044085.98256360.000.9176.14DN1251.35412.801.00管段3144085.98256360.000.9176.14DN1253.28412.801.00管段3243274.29251640.000.8973.47DN1255.61397.740.10管段3333597.59195370.001.06133.
7、15DN1004.33559.260.10管段3429074.81169070.000.92100.86DN1009.73418.820.10管段3524552.02142770.000.7773.00DN1004.32298.660.10管段3614875.3286500.000.81113.79DN804.28329.590.10管段3714875.3286500.000.81113.79DN804.30329.591.00管段3814875.3286500.000.81113.79DN801.13329.591.00管段3914875.3286500.000.81113.79DN801.
8、25329.591.00管段4010352.5460200.000.79134.65DN7012.80313.530.10管段414522.7926300.000.5799.38DN501.53162.151.50管段424522.7926300.000.5799.38DN500.25162.150.00管段435829.7533900.000.73160.68DN500.87269.410.10管段445829.7533900.000.73160.68DN505.41269.411.00管段455829.7533900.000.73160.68DN500.83269.411.00管段4658
9、29.7533900.000.73160.68DN500.25269.411.00管段474522.7926300.000.5799.38DN501.53162.151.50管段484522.7926300.000.5799.38DN500.25162.150.00管段499676.7056270.001.22424.25DN500.85742.291.50管段509676.7056270.001.22424.25DN500.25742.291.00管段514522.7926300.000.5799.38DN500.89162.151.50管段524522.7926300.000.5799.3
10、8DN500.25162.151.00管段534522.7926300.000.5799.38DN500.89162.151.50管段544522.7926300.000.5799.38DN500.25162.151.00管段559676.7056270.001.22424.25DN500.85742.291.50管段569676.7056270.001.22424.25DN500.25742.291.00管段57811.694720.000.64407.15DN201.15202.101.50管段58811.694720.000.64407.15DN200.25202.101.504.計(jì)算匯
11、總當(dāng)前最不利環(huán)路的阻力損失為43975.03 Pa。Pd(Pa)Pl(Pa)P(Pa)123.16466.13589.29681.11204.34885.46474.72320.05794.761216.653160.874377.5246.14138.74184.88461.42132.82594.24461.42472.70934.12461.42175.98637.4164.702090.532155.2333.56810.51844.0722.56378.77401.33243.23549.02792.25162.15152.55314.71502.6824.85527.52303.1
12、5460.69763.84303.1581.43384.58626.51101.79728.301113.43352.131465.563043.37106.063149.44404.12133.64537.761104.5940.171144.761113.43352.131465.563043.37106.063149.44243.23152.55395.79502.6824.85527.52510.79271.82782.60527.0024.85551.85486.46152.55639.02502.6824.85527.52619.2063.79682.98412.80103.115
13、15.90412.80249.61662.4139.77412.19451.9755.93575.87631.7941.88981.401023.2829.87315.74345.60供水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水力計(jì)算表32.96487.14520.10329.59489.79819.38329.59128.
14、48458.07329.59142.64472.2331.351723.551754.90243.23152.55395.79502.6824.85527.5226.94139.71166.65269.41869.251138.67269.41132.64402.051104.5940.171144.76243.23152.55395.79502.6824.85527.521113.43360.621474.043043.37106.063149.44243.2388.68331.91664.8324.85689.68243.2388.68331.91664.8324.85689.681113
15、.43360.621474.043043.37106.063149.44303.15467.43770.58929.67101.791031.454.計(jì)算匯總當(dāng)前最不利環(huán)路的阻力損失為43975.03 Pa?;厮芷矫鎴D水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水力計(jì)算表 編號(hào) 流量(kg/h) 負(fù)荷(w) 流速(m/s)Rm(Pa/m
16、)管徑 長(zhǎng)(m)動(dòng)壓(Pa) 管段088171.97512720.001.28117.57DN1501.03821.480.15管段144085.98256360.000.9175.30DN1255.80413.001.65管段24522.7926300.000.5797.83DN501.80162.231.50管段34522.7926300.000.5797.83DN501.53162.231.00管段44522.7926300.000.5797.83DN500.40162.230.00管段539563.20230060.001.25180.89DN1003.92775.881.50管段63
17、8751.50225340.001.22173.76DN1002.49744.371.50管段729074.81169070.000.9299.75DN1007.00419.030.10管段823245.06135170.000.7364.93DN1009.92267.840.10管段99676.7056270.001.22420.37DN500.60742.651.50管段109676.7056270.001.22420.37DN500.40742.651.00管段1113568.3678900.000.7494.26DN801.29274.350.10管段1213568.3678900.0
18、00.7494.26DN804.27274.351.00管段1313568.3678900.000.7494.26DN801.20274.351.00管段1413568.3678900.000.7494.26DN801.45274.351.00管段159045.5752600.000.69102.74DN7021.19239.480.10管段164522.7926300.000.5797.83DN502.43162.231.50管段174522.7926300.000.5797.83DN500.40162.230.00管段184522.7926300.000.5797.83DN501.5416
19、2.231.50管段194522.7926300.000.5797.83DN500.40162.230.00管段204522.7926300.000.5797.83DN501.54162.231.50管段214522.7926300.000.5797.83DN500.40162.230.00管段225829.7533900.000.73158.54DN500.60269.541.50管段235829.7533900.000.73158.54DN500.40269.541.00管段249676.7056270.001.22420.37DN500.60742.651.50管段259676.7056
20、270.001.22420.37DN500.40742.651.00管段26811.694720.000.64400.91DN201.10202.200.10管段27811.694720.000.64400.91DN200.20202.201.50管段28811.694720.000.64400.91DN200.40202.200.00管段2944085.98256360.000.9175.30DN1259.83413.000.25管段3044085.98256360.000.9175.30DN1252.79413.001.15管段3138256.23222460.001.20169.48DN
21、1005.41725.460.25管段3238256.23222460.001.20169.48DN1000.37725.461.15管段3333733.45196160.001.06132.85DN10012.80564.070.25管段344522.7926300.000.5797.83DN501.53162.231.50管段354522.7926300.000.5797.83DN500.40162.230.00管段3629210.66169860.000.92100.65DN1001.45422.950.25管段3729210.66169860.000.92100.65DN1001.13
22、422.951.15管段3829210.66169860.000.92100.65DN1004.30422.951.15管段3929210.66169860.000.92100.65DN1004.28422.951.15管段4019533.96113590.001.07189.91DN804.02568.630.25管段4115011.1887290.000.82114.39DN8010.03335.800.25管段4210488.3960990.000.80136.34DN704.03321.970.25管段43811.694720.000.64400.91DN205.61202.200.2
23、5管段44811.694720.000.64400.91DN201.12202.201.65管段45811.694720.000.64400.91DN200.40202.201.50管段469676.7056270.001.22420.37DN500.62742.651.50管段479676.7056270.001.22420.37DN500.40742.651.00管段484522.7926300.000.5797.83DN500.69162.231.50管段494522.7926300.000.5797.83DN500.40162.231.00管段504522.7926300.000.57
24、97.83DN500.69162.231.50管段514522.7926300.000.5797.83DN500.40162.231.00管段529676.7056270.001.22420.37DN500.62742.651.50管段539676.7056270.001.22420.37DN500.40742.651.00管段544522.7926300.000.5797.83DN501.53162.231.50管段554522.7926300.000.5797.83DN500.40162.230.00管段565829.7533900.000.73158.54DN500.30269.541.
25、50管段575829.7533900.000.73158.54DN500.40269.541.004.計(jì)算匯總當(dāng)前最不利環(huán)路的阻力損失為14913.14 Pa。Pd(Pa)Pl(Pa)P(Pa)123.22121.18244.40681.45436.731118.18243.35176.35419.70162.23150.16312.40243.3539.13282.481163.81709.221873.041116.55432.671549.2241.90698.23740.1326.78644.09670.881113.97252.221366.201856.62168.152024.7
26、727.43121.60149.03274.35402.56676.91274.35113.11387.46274.35136.93411.2823.952177.522201.46243.35238.21481.56243.3539.13282.48243.35150.16393.51243.3539.13282.48243.35150.16393.51243.3539.13282.48404.3295.72500.03673.8663.42737.281113.97252.221366.201856.62168.152024.7720.22440.88461.10303.3080.1838
27、3.48303.30160.36463.66103.25739.96843.21474.95210.08685.03181.37916.901098.27834.2862.76897.04141.021700.541841.56243.35150.16393.51243.3539.13282.48回水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算
28、結(jié)果平面圖水管水力計(jì)算表105.74146.21251.95486.40113.64600.04486.40433.20919.60486.40430.86917.25142.16764.39906.5483.951147.301231.2580.49548.75629.2450.552249.102299.65333.63447.52781.15606.60160.36766.961113.97260.631374.601856.62168.152024.77243.3567.81311.16405.5839.13444.72243.3567.81311.16405.5839.13444.7
29、21113.97260.631374.601856.62168.152024.77243.35150.16393.51243.3539.13282.48404.3247.17451.48673.8663.42737.284.計(jì)算匯總當(dāng)前最不利環(huán)路的阻力損失為14913.14 Pa。供水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水
30、力計(jì)算表 編號(hào) 流量(kg/h) 負(fù)荷(w) 流速(m/s)Rm(Pa/m)管徑 長(zhǎng)(m)動(dòng)壓(Pa) 管段085767.84498740.001.25112.41DN1503.93776.910.15管段144085.98256360.000.9176.14DN1250.79412.801.50管段244085.98256360.000.9176.14DN1251.40412.801.00管段344085.98256360.000.9176.14DN1253.33412.801.00管段443274.29251640.000.8973.47DN1255.61397.740.10管段53359
31、7.59195370.001.06133.15DN1004.33559.260.10管段629074.81169070.000.92100.86DN1009.73418.820.10管段724552.02142770.000.7773.00DN1004.32298.660.10管段814875.3286500.000.81113.79DN804.21329.590.10管段914875.3286500.000.81113.79DN804.35329.591.00管段1014875.3286500.000.81113.79DN801.20329.591.00管段1114875.3286500.0
32、00.81113.79DN801.25329.591.00管段124522.7926300.000.5799.38DN501.53162.151.50管段134522.7926300.000.5799.38DN500.25162.150.00管段1410352.5460200.000.79134.65DN7012.80313.530.10管段154522.7926300.000.5799.38DN501.53162.151.50管段164522.7926300.000.5799.38DN500.25162.150.00管段175829.7533900.000.73160.68DN500.942
33、69.410.10管段185829.7533900.000.73160.68DN505.41269.411.00管段195829.7533900.000.73160.68DN500.90269.411.00管段205829.7533900.000.73160.68DN500.25269.411.00管段219676.7056270.001.22424.25DN500.81742.291.50管段229676.7056270.001.22424.25DN500.25742.291.00管段234522.7926300.000.5799.38DN500.85162.151.50管段244522.7
34、926300.000.5799.38DN500.25162.151.00管段254522.7926300.000.5799.38DN500.85162.151.50管段264522.7926300.000.5799.38DN500.25162.151.00管段279676.7056270.001.22424.25DN500.81742.291.50管段289676.7056270.001.22424.25DN500.25742.291.00管段29811.694720.000.64407.15DN201.11202.101.50管段30811.694720.000.64407.15DN200.
35、25202.101.50管段3141681.86242380.001.31201.87DN1001.48860.781.50管段3241681.86242380.001.31201.87DN1004.20860.781.00管段334522.7926300.000.5799.38DN501.53162.151.50管段344522.7926300.000.5799.38DN500.25162.150.00管段3537159.07216080.001.17161.68DN1001.82684.110.10管段3637159.07216080.001.17161.68DN1001.20684.11
36、1.00管段3737159.07216080.001.17161.68DN10020.03684.111.00管段385829.7533900.000.73160.68DN501.59269.411.50管段395829.7533900.000.73160.68DN500.25269.410.00管段4031329.32182180.000.99116.40DN1000.04486.290.10管段4131329.32182180.000.99116.40DN1005.50486.290.00管段42811.694720.000.64407.15DN201.15202.100.10管段4381
37、1.694720.000.64407.15DN200.20202.101.50管段44811.694720.000.64407.15DN200.25202.100.00管段4530517.63177460.000.96110.68DN1002.79461.421.50管段4620840.93121190.001.14217.31DN809.62646.950.10管段4715011.1887290.000.82115.79DN807.00335.630.10管段485334.4831020.000.67135.76DN502.79225.580.10管段494522.7926300.000.5
38、799.38DN505.50162.151.50管段504522.7926300.000.5799.38DN501.54162.151.00管段514522.7926300.000.5799.38DN500.25162.150.00管段52811.694720.000.64407.15DN201.15202.101.50管段53811.694720.000.64407.15DN200.20202.101.50管段54811.694720.000.64407.15DN200.25202.100.00管段559676.7056270.001.22424.25DN500.85742.291.50管段
39、569676.7056270.001.22424.25DN500.25742.291.00管段575829.7533900.000.73160.68DN500.85269.411.50管段585829.7533900.000.73160.68DN500.25269.411.00管段599676.7056270.002.041604.34DN400.852072.711.50管段609676.7056270.001.22424.25DN500.25742.291.004.計(jì)算匯總當(dāng)前最不利環(huán)路的阻力損失為45703.15 Pa。Pd(Pa)Pl(Pa)P(Pa)116.54441.76558.2
40、9619.2059.86679.05412.80106.27519.07412.80253.54666.3439.77412.19451.9755.93575.87631.7941.88981.401023.2829.87315.74345.6032.96479.07512.03329.59494.53824.11329.59136.55466.14329.59142.64472.23243.23152.55395.79502.6824.85527.5231.351723.551754.90243.23152.55395.79502.6824.85527.5226.94151.72178.66
41、269.41869.251138.67269.41144.65414.061104.5940.171144.761113.43343.651457.073043.37106.063149.44243.2384.55327.78664.8324.85689.68243.2384.55327.78664.8324.85689.681113.43343.651457.073043.37106.063149.44303.15450.49753.64929.67101.791031.451291.17299.541590.70860.78848.561709.33243.23152.55395.7950
42、2.6824.85527.5268.41293.70362.11供水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水力計(jì)算表684.11194.02878.13684.113238.923923.03404.12255.47659.59835.1840.17875.3548.635.1253.750.00640.45640.4520
43、.21469.76489.97303.1581.43384.58626.51101.79728.30692.13308.801000.9464.702090.532155.2333.56810.51844.0722.56378.77401.33243.23546.81790.04162.15152.55314.71502.6824.85527.52303.15469.76772.91303.1581.43384.58626.51101.79728.301113.43360.621474.043043.37106.063149.44404.12137.22541.341104.5940.1711
44、44.763109.071363.694472.763043.37106.063149.444.計(jì)算匯總當(dāng)前最不利環(huán)路的阻力損失為45703.15 Pa。回水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水力計(jì)算表 編號(hào) 流量(kg/h) 負(fù)荷(w) 流速(m/s)Rm(Pa/m)管徑 長(zhǎng)(m)動(dòng)壓(Pa) 管段085767.844
45、98740.001.25111.43DN1501.03777.290.15管段144085.98256360.000.9175.30DN1259.75413.000.10管段244085.98256360.000.9175.30DN1252.81413.001.00管段338256.23222460.001.20169.48DN1005.41725.460.10管段438256.23222460.001.20169.48DN1000.45725.461.00管段54522.7926300.000.5797.83DN501.53162.231.50管段64522.7926300.000.5797
46、.83DN500.40162.230.00管段733733.45196160.001.06132.85DN10012.80564.070.10管段84522.7926300.000.5797.83DN501.53162.231.50管段94522.7926300.000.5797.83DN500.40162.230.00管段1029210.66169860.000.92100.65DN1001.45422.950.10管段1129210.66169860.000.92100.65DN1001.20422.951.00管段1229210.66169860.000.92100.65DN1004.3
47、5422.951.00管段1329210.66169860.000.92100.65DN1004.21422.951.00管段1419533.96113590.001.07189.91DN804.02568.630.10管段1515011.1887290.000.82114.39DN8010.03335.800.10管段1610488.3960990.000.80136.34DN704.03321.970.10管段17811.694720.000.64400.91DN205.61202.200.10管段18811.694720.000.64400.91DN201.07202.201.50管段1
48、9811.694720.000.64400.91DN200.40202.201.50管段209676.7056270.001.22420.37DN500.58742.651.50管段219676.7056270.001.22420.37DN500.40742.651.00管段224522.7926300.000.5797.83DN500.65162.231.50管段234522.7926300.000.5797.83DN500.40162.231.00管段244522.7926300.000.5797.83DN500.65162.231.50管段254522.7926300.000.5797.
49、83DN500.40162.231.00管段269676.7056270.001.22420.37DN500.58742.651.50管段279676.7056270.001.22420.37DN500.40742.651.00管段285829.7533900.000.73158.54DN500.37269.541.50管段295829.7533900.000.73158.54DN500.40269.541.00管段3041681.86242380.001.31200.17DN1005.78861.201.70管段314522.7926300.000.5797.83DN501.80162.23
50、1.50管段324522.7926300.000.5797.83DN501.54162.231.00管段334522.7926300.000.5797.83DN500.40162.230.00管段3437159.07216080.001.17160.19DN1003.90684.451.50管段3536347.38211360.001.14153.48DN1002.49654.871.50管段3626670.68155090.000.8484.50DN1007.00352.600.10管段3720840.93121190.001.14215.24DN809.92647.270.10管段3896
51、76.7056270.001.22420.37DN500.63742.651.50管段399676.7056270.001.22420.37DN500.40742.651.00管段4011164.2364920.000.85153.68DN702.49364.800.10管段4110352.5460200.000.79132.97DN705.77313.681.50管段424522.7926300.000.5797.83DN5019.50162.232.00管段434522.7926300.000.5797.83DN501.20162.231.00管段444522.7926300.000.57
52、97.83DN501.62162.231.00管段454522.7926300.000.5797.83DN501.23162.231.00管段464522.7926300.000.5797.83DN500.40162.230.00管段475829.7533900.000.73158.54DN501.59269.543.00管段485829.7533900.000.73158.54DN500.40269.540.00管段49811.694720.000.64400.91DN201.12202.201.50管段50811.694720.000.64400.91DN200.20202.201.50管
53、段51811.694720.000.64400.91DN200.40202.200.00管段525829.7533900.000.73158.54DN500.63269.541.50管段535829.7533900.000.73158.54DN500.40269.541.00管段549676.7056270.001.22420.37DN500.63742.651.50管段559676.7056270.001.22420.37DN500.40742.651.00管段56811.694720.000.64400.91DN201.12202.200.10管段57811.694720.000.6440
54、0.91DN200.20202.201.50管段58811.694720.000.64400.91DN200.40202.200.004.計(jì)算匯總當(dāng)前最不利環(huán)路的阻力損失為13972.00 Pa。Pd(Pa)Pl(Pa)P(Pa)116.59114.77231.3741.30734.33775.63413.00211.97624.9772.55916.90989.45725.4675.43800.89243.35150.16393.51243.3539.13282.4856.411700.541756.94243.35150.16393.51243.3539.13282.4842.30146.
55、21188.50422.95120.78543.73422.95437.39860.34422.95423.72846.6756.86764.39821.2533.581147.301180.8832.20548.75580.9520.222249.102269.32303.30430.84734.14606.60160.36766.961113.97243.821357.791856.62168.152024.77243.3563.74307.09405.5839.13444.72243.3563.74307.09405.5839.13444.721113.97243.821357.7918
56、56.62168.152024.77404.3259.02463.33673.8663.42737.281464.041155.962619.99243.35176.35419.70162.23150.16312.40243.3539.13282.481026.67624.501651.17982.31382.181364.48回水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl + Pd。c.Pdn P
57、d1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水力計(jì)算表35.26591.48626.7464.732135.212199.941113.97264.831378.811856.62168.152024.7736.48382.67419.15470.52767.781238.31324.471908.062232.53162.23117.39279.63162.23158.22320.45162.23120.82283.05243.3539.13282.48808.63252.081060.71404.3263.42467.73303.30449.81753.11303.3080.18383.
58、48303.30160.36463.66404.3299.25503.57673.8663.42737.281113.97264.831378.811856.62168.152024.7720.22449.81470.03303.3080.18383.48303.30160.36463.664.計(jì)算匯總當(dāng)前最不利環(huán)路的阻力損失為13972.00 Pa。供水管平面圖水力計(jì)算書1.計(jì)算依據(jù)本計(jì)算方法理論依據(jù)是陸耀慶編著的供暖通風(fēng)設(shè)計(jì)手冊(cè)和電子工業(yè)部第十設(shè)計(jì)研究院主編的空氣調(diào)節(jié)設(shè)計(jì)手冊(cè)。2.計(jì)算公式a.計(jì)算摩擦阻力系數(shù)的公式采用的是柯列勃洛克懷特公式。b.管段損失 沿程損失局部損失 即:Pg Pl
59、+ Pd。c.Pdn Pd1 (PmL Pz)。3.計(jì)算結(jié)果平面圖水管水力計(jì)算表 編號(hào) 流量(kg/h) 負(fù)荷(w) 流速(m/s)Rm(Pa/m)管徑 長(zhǎng)(m)動(dòng)壓(Pa) 管段018663.80108530.001.02175.73DN801.08518.840.15管段19647.4656100.000.74117.73DN7030.70272.281.50管段29647.4656100.000.74117.73DN7026.38272.281.00管段39647.4656100.000.74117.73DN702.50272.281.00管段41262.257340.000.61275
60、.75DN251.82187.521.50管段5631.133670.000.49253.91DN201.19122.181.50管段6631.133670.000.49253.91DN200.25122.180.00管段7631.133670.000.49253.91DN200.28122.181.50管段8631.133670.000.49253.91DN200.25122.180.00管段98385.2148760.000.6490.22DN704.36205.690.10管段10631.133670.000.49253.91DN201.78122.181.50管段11631.13367
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