末端最不利环路水力计算书

设计计算书项目名称换热站图号计算条件1，换热站设计规模为 1.5×105㎡，综合为指标55W/㎡。

最长环路长度为600米，无地形高差为。

2，一次网设计压力为 1.6Mpa，供回水设计温度为130/70℃（校核温度为110/60℃）；二次网设计压力为 1.0Mpa，设计温度为55/45℃。

采暖形式为地暖3、换热站为新建换热站，按有人值守站设计，水泵设变频。

计算内容水力计算一、最不利环路阻力损失计算（一）、外网总沿程阻力计算：最远建筑楼前热力入口至换热站600m，取管网平均比摩阻60Pa/m，计算损失：△h YC＝2×600×60=72000Pa=0.072Mpa（二）、局部阻力计算：局部阻力取沿程阻力的30％，即△h JB＝0.072Mpa×30％＝0.0216Mpa（三）、换热站内阻力损失：∑△h ZN＝0.10MPa（四）、用户压头损失：∑△h YH＝0.05 MPa（五）、总阻力计算：总阻力损失为：△h＝△h YC +△h JB +△h ZN +△h YH=0.072+0.0216+0.10+0.05=0.2436 MPa二、管径选择（一）一次网管径选择一次网母管的管径计算供热一次网设计供回水温度130℃/70℃，热负荷：55×1.5×105=8250kW。

则一次网设计流量：G1＝3.6×8250/(4.2×60)＝117.86t/h可选择一次网母管管径DN200校核温度为100℃/60℃校核流量为G 1＝3.6×8250/(4.2×40)＝176.79t/h可选择一次网母管管径DN200，△h ＝129.6Pa/m ，υ=1.14m/s 。

除污器旁通的管径（比主管小一号）取DN200（二）二次网管径选择二次网供回水温差△t 2=10℃（设计供水温度55/45℃），供热负荷为55×1.5×105=8250KW二次网循环水量：G 2＝3.6×8250/(4.2×10)＝707.14t/h选择二次网母管管径：DN400 ，△h ＝55.5Pa/m ，υ=1.52m/s 。

设计软件：浩辰暖通工程设计软件 鉴定信息：建设行业科技成果评估证书 建科评[2009]062号
垂直采暖水力计算书
分支1水力计算表
分支1-立管1水力计算表
分支1-立管2水力计算表
分支1-立管3水力计算表
分支1-立管4水力计算表
分支1-立管5水力计算表
分支1-立管6水力计算表
分支1-立管7水力计算表
分支2水力计算表
分支2-立管1水力计算表
分支2-立管2水力计算表
分支2-立管3水力计算表
分支2-立管4水力计算表
分支2-立管5水力计算表
分支2-立管6水力计算表
分支2-立管7水力计算表
分支2-立管8水力计算表
算书。

表1 系统最不利环路水力计算表
表2 总供回水干管水力计算表
表3 分支1供回水干管水力计算表
表4 分支1立管1供回水立管水力计算表
表5 分支1立管2供回水立管水力计算表
表6 分支1立管3供回水立管水力计算表
表7 分支1立管4供回水立管水力计算表
表8 分支1立管5供回水立管水力计算表
表9 分支2供回水干管水力计算表
表10 分支2立管1供回水立管水力计算表
表11 分支2立管2供回水立管水力计算表
表12 分支2立管3供回水立管水力计算表
表13 分支2立管4供回水立管水力计算表
表14 分支2立管5供回水立管水力计算表
表15 分支2立管6供回水立管水力计算表。

二、并联环路：
管段1：闸阀0.08+90°焊接弯头0.72+合流三通0.1=0.9
管段2：水过滤器2.0+焊接弯头0.78×2=3.56
管段3：直流三通0.1+闸阀0.08×2+止回阀3.4=3.36
管段4：变径0.1×2+90°焊接弯头0.78×3=2.54
管段5：闸阀0.08×2+90°焊接弯头0.78×2=1.88
管段6：变径0.1+直流三通0.1+90°焊接弯头0.72+闸阀0.08=1 管段1’：闸阀0.08+90°焊接弯头0.72×2=1.52
管段6'：90°焊接弯头0.72×2+闸阀0.08=1.52
冷冻水系统：
四．并联环路：
最不利环路总损失：68760.592Pa
局部阻力系数：
管段1：闸阀0.08+90°焊接弯头0.72+直流三通0.1=0.9
管段2：直流三通0.1+闸阀0.08×2+止回阀3.4=3.66
管段3：水过滤器 2.0+90°焊接弯头0.72+直流三通（旁流三通）1.6+变径0.1=4.42
管段4：90°焊接弯头0.78+闸阀0.08=0.86
管段5：90°焊接弯头0.78+闸阀0.08=0.86
管段6：闸阀0.08+变径0.1+直流三通0.1+90°焊接弯头0.72×2=1.72
管段1'=闸阀0.08+90°焊接弯头0.72×5+三通1.5=2.3
管段6':闸阀0.08+三通1.5+90°焊接弯头0.72×2+变径0.1=3.12。

水力计算说明书一．风管水力计算风管压力损失计算的根本任务是解决如下两个问题：设计计算和校核计算。

确定好设备布置、风量、管道走向等之后，应经济合理地确定风管的断面尺寸，以保证实际风量符合设计要求；计算系统总阻力，以确定风机的型号及相应的电机；计算风机及相应电机是否满足要求。

本设计中，风管压力损失计算根据《实用供热空调设计手册》风管计算方法来确定。

水力计算的方法及步骤如下：(1)计算步骤：①绘制空调系统轴测图,并对各段风管进行编号,标注。

②设定风管内的合理流速。

③根据各风管的风量和选择的流速确定各管段的断面尺寸,计算沿程阻力和局部阻力。

④与最不利环路并联的管路的阻力平衡计算。

为了保证各送风点达到预期的风量，必须进行阻力平衡计算。

一般的空调系统要求并联管路之间的不平衡率应不超过15%。

若超出上述规定，则应采用下面几种方法使其阻力平衡。

①在风量不变的情况下，调整支管管径；②在支管断面尺寸不变情况下，适当调整支管风量； ③在风量不变的情况下，在支管加平衡阀。

(2)系统总阻力的计算计算风管的压力损失：通过对风管的沿程压力损失和局部压力损失的计算，最终确定风管的尺寸。

①矩形风管截面积：3600×=V LS其中：L 为风管的流量，单位：m³/hV 为风管假定的流速，单位：m/s ，本设计中取V=9m/s ②沿程压力损失:L R P m m =Δ其中：R m 为单位长度的比摩阻， Pa/mL 为管长，m③局部压力损失：2ρξp 2m v =其中：ξ为局部阻力系数；ρ为空气的密度，kg/m 3ν与ξ对应的风道断面平均速度，m/s 。

④风管的压力损失s j m P P P P ΔΔΔΔ++= 其中，sP Δ为风系统设备阻力，Pa 。

(2)计算最不利环路的压力损失 计算结果如下：各机组出口送风管管径汇总风管管径空调机组楼层设备型号 送风量m3/h 制冷量KW 机组管径 长*宽 实际流速 覆盖区域散流器个数负一层KBG50-4 8623.8 135 630*320 11.13 9 KBG80-6 8623.8 135 800*320 10.65 9 KBG120-4 11498.4 180 1000*400 9.98 12 KBG70-4 7665.6 120 800*320 10.45 8 KBG70-4 5749.2 90 630*320 11.09 6 KBG80-4 8623.8 135 800*320 10.87 9 KBG60-4 5749.2 90 630*320 11.02 6 KBG80-4 5749.2 90 630*320 10.78 6 KBG70-4 7665.6 120 630*320 10.34 8 KBG70-4 7665.6 120 630*320 10.75 8 KBG70-4 7665.6 120 630*320 10.35 8 KBG100M-4 14373 225 1000*400 9.57 15 KBG140-4 14373 225 1000*400 9.43 15 KBG70-4 7665.6 120 630*320 10.57 8 KBG70M-4 4791 75 630*320 11.01 5 一层KBG120-6 15264.2 229.6 800*400 12.02 14 KBG120-4 15264.2 229.6 1000*400 11.93 14 KBG80-4 9812.7 147.6 1000*320 10.83 9 KBG80-4 11993.3 180.4 800*320 11.59 11 KBG80-4 10903 164 630*320 12.45 10 KBG80-49812.7147.6800*32010.379KBG80-4 10903 164 800*320 11.21 10二、三、四层KBG120-6 14028 208.8 800*320 10.98 12 KBG120-4 15197 226.2 1000*320 9.84 13 KBG120-4 17535 261 1000*400 9.43 15 KBG100M-4 14028 208.8 1000*400 9.24 12 KBG100-6 17535 261 1000*320 9.57 15 KBG100-4 11690 174 1000*400 9.62 10 KBG100-6 18704 278.4 800*320 11.06 16五层KBG80-6 17075 408 800*320 13.04 10 KBG80-6 15367.5 367.2 800*320 12.51 9 KBG120-6 15367.5 367.2 1000*400 11.69 9 KBG100-6 13660 326.4 800*320 12.7 8 KBG100-6 17075 408 800*320 12.07 10新风机组一层KBG50N-4 15921 180 800*320 12.23 11 KBG60N-4 39079 441.2 800*320 13.07 17全热换热器一层CHA-D8000 15921 180 800*320 12.23 10 CHA-D8000 39079 441.2 800*320 13.07 11二层CHA-D8000 54359 809 800*320 11.93 11 CHA-D8000 54359 809 800*320 12.56 11三层CHA-D8000 54359 809 800*320 12.73 11 CHA-D8000 54359 809 800*320 12.99 11四层CHA-D8000 62778 1866 800*320 13.51 11 CHA-D8000 62778 1866 800*320 11.96 11五层CHA-D000 378 1866 630*320 13.51 0 CHA-D8000 78546 1866 800*450 11.96 12水力计算结果分支1最不利路径水力计算表最不利阻力(Pa)458编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 25270 10.95 矩形1000 400 12.73 15.84 88.23 104.072 21235.5 1.03 矩形800 320 7.62 0.71 71.26 71.973 7890 3.4 矩形800 320 6.99 2.32 122.53 124.844 5607 3.4 矩形800 320 4.23 0.78 21.99 22.775 1105 1.38 矩形320 250 6.77 2.72 113.72 116.446 1105 3.4 矩形320 250 2.64 1 5.88 6.887 1105 0.15 矩形320 200 2.64 0.04 11.43 11.47分支1水力计算表编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 2728 10.95 矩形1000 400 12.73 15.84 88.23 104.072 2635 1.03 矩形800 320 7.62 0.71 71.26 71.973 21235.5 3.4 矩形800 320 6.99 2.32 122.53 124.844 7890 3.4 矩形800 320 4.23 0.78 21.99 22.775 5607 3.4 矩形800 320 4.74 1.32 55.72 57.046 1105 3.4 矩形500 320 4.33 1.43 13.97 15.417 1105 1.22 矩形500 320 4.33 0.85 12.16 138 1105 3.5 矩形320 250 3.39 1.9 8.26 10.169 569 0.15 矩形320 250 3.39 0.08 18.72 18.810 569 0.25 矩形320 250 3.39 0.14 30.02 30.1611 1103 1.38 矩形500 320 4.33 0.96 11.7 12.66分支1平衡分析表18.72 18.8编号不平衡率总阻力并联最不利阻力平衡阀阻力2 0 354.37 354.37 03 0 282.4 282.4 0分支2最不利路径水力计算表最不利阻力(Pa)646编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 34267 1.35 矩形1000 400 16.25 3.12 143.78 146.92 34267 1.35 矩形1000 320 15.98 3.03 0 3.033 3567 0.76 矩形630 320 10.58 2.99 277.63 280.624 2307 1.54 矩形630 250 10.16 6.54 126.68 133.235 1105 0.96 矩形320 250 6.77 1.9 57.14 59.046 569 1.4 矩形320 250 2.64 0.41 5.88 6.297 569 1.05 矩形320 250 2.64 0.31 4.87 5.188 569 0.15 矩形320 250 2.64 0.04 11.43 11.47分支2水力计算表编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 34267 1.35 矩形1000 400 16.25 3.12 143.78 146.92 34267 1.35 矩形1000 320 15.98 3.03 0 3.033 3567 0.76 矩形800 320 10.16 2.11 17.47 19.584 2307 3.4 矩形630 320 5.42 2.51 72.78 75.295 1105 3.4 矩形500 250 4.33 2.36 1.65 4.016 569 0.94 矩形320 250 3.39 0.51 8.26 8.777 569 0.15 矩形320 250 3.39 0.08 18.72 18.88 569 1.16 矩形320 250 3.39 0.63 12.55 13.189 569 0.15 矩形320 250 3.39 0.08 18.72 18.810 569 0.94 矩形400 250 2.71 0.3 22.92 23.2211 569 0.15 矩形500 250 2.17 0.03 7.67 7.712 569 1.16 矩形400 250 2.71 0.37 22.92 23.2913 569 0.15 矩形500 250 2.17 0.03 7.67 7.714 569 1.16 矩形500 250 2.17 0.22 15.08 15.31分支2平衡分析表编号不平衡率总阻力并联最不利阻力平衡阀阻力2 0 498.85 498.85 0分支3最不利路径水力计算表最不利阻力(Pa)304编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 2728 1.08 矩形1000 400 8.13 0.74 82.83 83.582 2635 1.92 矩形1000 320 8.13 1.31 0 1.313 21235.5 7.89 矩形800 320 5.5 2.94 2.67 5.614 7890 1.45 矩形800 320 4.84 0.5 0 0.55 5607 3.4 矩形630 320 4.78 1.3 1.82 3.126 1105 3.4 矩形630 320 5.37 2.2 2.4 4.67 1105 3.4 矩形200 200 13.54 38.14 21.41 59.568 1105 1.11 矩形200 200 6.77 3.34 67.4 70.749 569 0.15 矩形200 200 6.77 0.45 74.89 75.34分支3水力计算表编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 2728 1.08 矩形1000 400 8.13 0.74 82.83 83.582 2635 7.89 矩形800 320 5.5 2.94 2.67 5.613 21235.5 1.45 矩形800 320 4.84 0.5 0 0.54 7890 3.4 矩形630 320 4.78 1.3 1.82 3.125 5607 3.4 矩形630 320 5.37 2.2 2.4 4.66 1105 3.4 矩形200 200 13.54 38.14 21.41 59.567 1105 1.11 矩形200 200 6.77 3.34 67.4 70.748 1105 0.15 矩形200 200 6.77 0.45 74.89 75.349 569 1.1 矩形200 200 6.77 3.3 81.54 84.8410 569 1.29 矩形320 250 5.29 1.36 34.19 35.5611 1103 0.17 矩形320 250 2.64 0.05 5.88 5.9312 569 1.02 矩形320 250 2.64 0.3 4.87 5.1713 569 0.15 矩形320 250 2.64 0.04 11.43 11.4714 569 0.25 矩形320 200 2.64 0.07 16.84 16.9215 569 1.11 矩形250 200 3.39 0.6 22.16 22.77分支3平衡分析表编号不平衡率总阻力并联最不利阻力平衡阀阻力2 0 220.78 220.78 03 0 219.46 219.46 04 0.63 80.36 219.46 139.1分支4最不利路径水力计算表最不利阻力(Pa)684编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 2728 0.73 矩形1000 320 15.44 1.52 301.8 303.322 1987 4.56 矩形800 302 15.44 9.56 0 9.563 986 1.05 矩形650 320 11.1 1.17 155.91 157.084 569 3.4 矩形500 320 9.75 2.95 7.6 10.55分支4水力计算表编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 2728 0.73 矩形1000 320 15.44 1.52 301.8 303.322 1987 4.56 矩形800 302 15.44 9.56 0 9.563 986 1.05 矩形650 320 11.1 1.17 155.91 157.084 569 3.4 矩形500 320 9.75 2.95 7.6 10.555 569 3.4 矩形500 320 8.4 2.22 5.71 7.936 569 3.4 矩形500 320 7.04 1.59 34.2 35.797 569 3.4 矩形320 200 7.11 1.81 4 5.818 569 3.4 矩形320 200 6.77 1.87 31.34 33.229 569 3.4 矩形320 200 5.08 1.09 2.26 3.35分支4平衡分析表编号不平衡率总阻力并联最不利阻力平衡阀阻力2 0 380.7 380.7 03 0 371.15 371.15 04 0.42 216.45 371.15 154.7分支5最不利路径水力计算表最不利阻力(Pa)518编号G(kg/h) L(m) 形状D/W(mm) H(mm) υ(m/s)ΔPy(Pa)ΔPj(Pa)ΔP(Pa)1 2831 3.4 矩形1000 400 6.5 1.37 3.43 4.83 1769.25 3.4 矩形800 320 6.35 1.66 3.17 4.834 1258 1.69 矩形320 250 7.93 3.82 171.02 174.845 1258 3.7 矩形320 250 5.29 3.91 17.94 21.866 569 3.4 矩形320 250 2.64 1 5.88 6.887 569 0.15 矩形320 250 2.64 0.04 11.43 11.47分支5水力计算表编号 G(kg/h) L(m) 形状 D/W(mm) H(mm) υ(m/s) ΔPy(Pa) ΔPj(Pa) ΔP(Pa) 1 2831 3.4 矩形 1000 320 6.77 1.65 3.7 5.35 2 1769.25 3.4 矩形 800 320 6.35 1.66 3.17 4.83 3 1258 3.4 矩形 800 320 4.23 0.78 1.66 2.44 4 1258 3.4 矩形 800 320 4.23 1.27 44.75 46.01 5 569 0.91 矩形 320 250 5.29 0.97 68.73 69.7 6 569 1.69 矩形 320 250 7.93 3.82 171.02 174.84 7 491 3.7 矩形 320 250 5.29 3.91 17.94 21.86 8 491 3.4 矩形 320 250 2.64 1 5.88 6.88 9 491 0.15矩形 320 250 2.640.0411.43 11.47 分支5平衡分析表编号 不平衡率 总阻力 并联最不利阻力 平衡阀阻力 2 0 275.55 275.55 0 3 0 269.78 269.78 040.42155.55269.78114.24二．水管水力计算空调水系统水管管径由下式确定：式中 0m ——管道中水流量，s m 3； v ——管道中水流速，s m 。

空调风系统水力计算书一、 计算依据《实用供热空调设计手册》第二版 风系统基本参数:气温(℃): 20 ; 大气压力(Pa): 843.8 ; 管材:薄钢板; 绝对粗糙度(米米):0.16;干管推荐流速上限(米/s):10. 干管推荐流速下限(米/s):4..;支管推荐流速上限(米/s):6.; 支管推荐流速下限(米/s):2.;运动粘度(米^2/s):1.57E-05二、 计算公式1. 沿程阻力(Pa)22v d l P m ρλ⋅⋅=∆2. 局部阻力(Pa)22v P j ρζ⋅=∆三、 计算结果1、 PFY.B3(1)-1排风系统1.1 根据地下室空调风管平面图,该风系统最不利环路的水力计算如下:负二层排风管(PFY.B2(4)-1)水力计算表1.2 风系统阻力计算对于地下负二层排风管(PFY.B2(4)-1):P＝沿程阻力+局部阻力+末端风口阻力+消声器阻力＝64.7+180.1+30+50＝324.8Pa风机压头校核:324.8*1.1=357Pa<400Pa,风机选型满足要求.2、XF.(2)C1-1新风系统2.1根据空调风管平面图,该风系统最不利环路的水力计算如下:商业C新风管(XF.(2)C1-1)水力计算表2.2风系统阻力计算商业C新风管(XF.(2)C1-1):P＝沿程阻力+局部阻力+消声器阻力＝19.7+202+50＝272Pa风机压头校核:272*1.1=299Pa<300Pa,风机选型满足要求.3、风机单位风量耗功率计算(1)计算公式W S=P/(3600×ηCD×ηF)式中:W S—风道系统单位风量耗功率[W/(米³/h)]; P—空调机组的余压或通风系统风机的风压(Pa); ηCD—电机及传动效率(%),ηCD取0.855;ηF—风机效率(%),按设计图中标注的效率选择.(2)计算结果选取PFY.B3(1)-1系统为例,则W S＝P/(3600η)＝500/(3600*0.855*0.75)＝0.22附件：工程施工现场应急预案及安全保证措施一、编制原则1、以人为本,安全第一原则。

85983.28楼层数6立管形式单管立管数29立管关系编号表1表2表3表4表5表6表7表8表9表10表11表12表13表14表15表16表17表18表19表20表21表22表23表24表25表26表27表28表29表30表31表32表33表34采暖系统水力计算书热媒系统形式分支2立管13供回水立管水力计算表散热器选型计算表表1 系统最不利环路水力计算表分支2立管7供回水立管水力计算表分支2立管8供回水立管水力计算表分支2立管9供回水立管水力计算表分支2立管10供回水立管水力计算表分支2立管11供回水立管水力计算表分支2立管12供回水立管水力计算表分支2立管1供回水立管水力计算表分支2立管2供回水立管水力计算表分支2立管3供回水立管水力计算表分支2立管4供回水立管水力计算表分支2立管5供回水立管水力计算表分支2立管6供回水立管水力计算表分支1立管12供回水立管水力计算表分支1立管13供回水立管水力计算表分支1立管14供回水立管水力计算表分支1立管15供回水立管水力计算表分支1立管16供回水立管水力计算表分支2供回水干管水力计算表分支1立管6供回水立管水力计算表分支1立管7供回水立管水力计算表分支1立管8供回水立管水力计算表分支1立管9供回水立管水力计算表分支1立管10供回水立管水力计算表分支1立管11供回水立管水力计算表分支1供回水干管水力计算表分支1立管1供回水立管水力计算表分支1立管2供回水立管水力计算表分支1立管3供回水立管水力计算表分支1立管4供回水立管水力计算表分支1立管5供回水立管水力计算表最不利损失(Pa16431表格目录表格名称系统最不利环路水力计算表总供回水干管水力计算表供回水方式上供下回同程总负荷(W190719.1总流量(kg/h8200.92工程名称单管-同程采暖系统供水温度(℃回水温度(℃65平均密度(kg/m3运动黏度(10-6m2/s0.479最不利阻力(Pa16431最不利环路分支1立管2编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaSG190719.18200.9210700.6480.820808SH190719.18200.9210700.6480.820808SG1190719.18200.924700.6480.82 1.6323SG2190719.18200.92050 1.05295.77 1.60BG1101146.224349.292500.5685.470171BG288913.243823.27 3.82500.4966.540.1254BH16101146.224349.2962.99500.5685.4705384BH1588917.713823.462500.4966.550.1133BH1483696.513598.95 5.21500.4659.180.1308BH1378475.313374.442500.4352.250.1104 BH1273253.693149.91 4.98500.445.740.1228 BH1168032.372925.392500.3739.660.179BH1062811.012700.87 4.99500.3534.020.1170 BH957589.692476.362400.53108.240.1216 BH852368.462251.84 5.1400.4890.010.1459 BH747147.242027.332400.4373.450.1147BH6419261802.82 4.94400.3958.560.1289 BH536704.781578.312320.4491.960.1184BH431023.431334.01 5.32320.3866.480.1354 BH325342.081089.719.66320.3145.090.1436 BH218787.53807.86 3.69250.4107.960.1398 VG16554.55281.85 2.2200.2249.61 1.5109 VG26554.55281.85 3.1200.2249.610154VG36554.55281.85 3.1200.2249.610154VG46554.55281.85 3.1200.2249.610154VG56554.55281.85 3.1200.2249.610154VG66554.55281.85 3.1200.2249.610154VH16554.55281.850.5200.2249.61 1.525R11078.5281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R12098.25281.851150.41233.033233表2 总供回水干管水力计算表编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(Pa SG190719.18200.9210700.6480.820808SH190719.18200.9210700.6480.820808SG1190719.18200.924700.6480.82 1.6323SG189572.883851.634700.318.740.375SG2190719.18200.92050 1.05295.77 1.60SG289572.883851.630500.4967.50.30表3 分支1供回水干管水力计算表编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(Pa BG1101146.224349.292500.5685.470171BG288913.243823.27 3.82500.4966.540.1254BG382358.693541.42 3.69500.4557.370.1212BG475804.143259.589.66500.4248.870.1472 BG570122.793015.282500.3942.050.184BG664441.442770.98 1.5500.3535.730.154 BG759220.212546.472400.54114.270.1229 BG853998.982321.96 1.53400.595.520.1146 BG948777.762097.442400.4578.440.1157 BG1043556.531872.93 1.52400.463.030.196 BG1138335.21648.412320.46100.030.1200 BG1233113.851423.9 1.59320.475.380.1120 BG1327892.531199.382320.3454.190.1108 BG1422670.91974.85 1.51320.2736.450.155 BG1517449.71750.342250.3793.650.1187 BG1612228.51525.83 2.85250.2647.440.1135 BH112232.98526.022250.2647.470.195BH218787.53807.86 3.69250.4107.960.1398 BH325342.081089.719.66320.3145.090.1436 BH431023.431334.01 5.32320.3866.480.1354 BH536704.781578.312320.4491.960.1184 BH6419261802.82 4.94400.3958.560.1289BH747147.242027.332400.4373.450.1147BH852368.462251.84 5.1400.4890.010.1459BH957589.692476.362400.53108.240.1216BH1062811.012700.87 4.99500.3534.020.1170BH1168032.372925.392500.3739.660.179BH1273253.693149.91 4.98500.445.740.1228BH1378475.313374.442500.4352.250.1104BH1483696.513598.95 5.21500.4659.180.1308BH1588917.713823.462500.4966.550.1133BH16101146.224349.2962.99500.5685.4705384表4 分支1立管1供回水立管水力计算表立管总阻力(Pa3498资用压力(Pa4021立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG112232.98526.02 2.2250.2647.47 1.5104VG212232.98526.02 3.1250.2647.470147VG312232.98526.02 3.1250.2647.470147VG412232.98526.02 3.1250.2647.470147VG512232.98526.02 3.1250.2647.470147VG612232.98526.02 3.1250.2647.470147VH112232.98526.020.5250.2647.47 1.524R22038.83526.021200.42163.443163R22038.83526.021200.42163.443163R22038.83526.021200.42163.443163R22038.83526.021200.42163.443163R22038.83526.021200.42163.443163R22038.83526.021200.42163.443163表5 分支1立管2供回水立管水力计算表立管总阻力(Pa3853本分支最不利立管编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(Pa VG16554.55281.85 2.2200.2249.61 1.5109VG26554.55281.85 3.1200.2249.610154VG36554.55281.85 3.1200.2249.610154VG46554.55281.85 3.1200.2249.610154VG56554.55281.85 3.1200.2249.610154VG66554.55281.85 3.1200.2249.610154VH16554.55281.850.5200.2249.61 1.525R11078.5281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R12098.25281.851150.41233.033233表6 分支1立管3供回水立管水力计算表立管总阻力(Pa3853资用压力(Pa4038立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16554.55281.85 2.2200.2249.61 1.5109VG26554.55281.85 3.1200.2249.610154VG36554.55281.85 3.1200.2249.610154VG46554.55281.85 3.1200.2249.610154VG56554.55281.85 3.1200.2249.610154VG66554.55281.85 3.1200.2249.610154VH16554.55281.850.5200.2249.61 1.525R11078.5281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R1844.45281.851150.41233.033233R12098.25281.851150.41233.033233表7 分支1立管4供回水立管水力计算表立管总阻力(Pa3565资用压力(Pa3997立管不平衡编号Q(W G(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15681.35244.3 2.2200.1937.89 1.583VG25681.35244.3 3.1200.1937.890.6117VG35681.35244.3 3.1200.1937.890.6117VG45681.35244.3 3.1200.1937.890.6117VG55681.35244.3 3.1200.1937.890.6117VG65681.35244.3 3.1150.35177.010.6549VH15681.35244.30.5150.35177.01 1.589R11225244.31150.35177.013177R1839.4244.31150.35177.013177R1839.4244.31150.35177.013177R1839.4244.31150.35177.013177R1839.4244.31150.35177.013177R11098.75244.31150.35177.013177表8 分支1立管5供回水立管水力计算表立管总阻力(Pa3780资用压力(Pa4267立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15681.35244.3 2.2200.1937.89 1.583VG25681.35244.3 3.1200.1937.890117VG35681.35244.3 3.1200.1937.890117VG45681.35244.3 3.1200.1937.890117VG55681.35244.3 3.1150.35177.010549VG65681.35244.3 3.1150.35177.010549VH15681.35244.30.5200.1937.89 1.519R21225244.31150.35177.013177R2839.4244.31150.35177.013177R2839.4244.31150.35177.013177R2839.4244.31150.35177.013177R2839.4244.31150.35177.013177R21098.75244.31150.35177.013177表9 分支1立管6供回水立管水力计算表立管总阻力(Pa3943资用压力(Pa4400立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.23224.51 2.2200.1832.34 1.571VG25221.23224.51 3.1200.1832.340100VG35221.23224.51 3.1150.33150.550467VG45221.23224.51 3.1150.33150.550467VG55221.23224.51 3.1150.33150.550467VG65221.23224.51 3.1150.33150.550467VH15221.23224.510.5200.1832.34 1.516R11129224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R11119.03224.511150.33150.553151表10 分支1立管7供回水立管水力计算表立管总阻力(Pa3943资用压力(Pa4454立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.23224.51 2.2200.1832.34 1.571VG25221.23224.51 3.1200.1832.340100VG35221.23224.51 3.1150.33150.550467VG45221.23224.51 3.1150.33150.550467VG55221.23224.51 3.1150.33150.550467VG65221.23224.51 3.1150.33150.550467VH15221.23224.510.5200.1832.34 1.516R21129224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R21119.03224.511150.33150.553151表11 分支1立管8供回水立管水力计算表立管总阻力(Pa3943资用压力(Pa4452立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.23224.51 2.2200.1832.34 1.571VG35221.23224.51 3.1150.33150.550467VG45221.23224.51 3.1150.33150.550467VG55221.23224.51 3.1150.33150.550467VG65221.23224.51 3.1150.33150.550467VH15221.23224.510.5200.1832.34 1.516R11129224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R11119.03224.511150.33150.553151表12 分支1立管9供回水立管水力计算表立管总阻力(Pa3943资用压力(Pa4755立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.23224.51 2.2200.1832.34 1.571VG25221.23224.51 3.1200.1832.340100VG35221.23224.51 3.1150.33150.550467VG45221.23224.51 3.1150.33150.550467VG55221.23224.51 3.1150.33150.550467VG65221.23224.51 3.1150.33150.550467VH15221.23224.510.5200.1832.34 1.516R21129224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R21119.03224.511150.33150.553151表13 分支1立管10供回水立管水力计算表立管总阻力(Pa4309资用压力(Pa4882立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.32224.52 2.2200.1832.34 1.571VG25221.32224.52 3.1150.33150.560467VG35221.32224.52 3.1150.33150.560467VG45221.32224.52 3.1150.33150.560467VG55221.32224.52 3.1150.33150.560467VG65221.32224.52 3.1150.33150.560467VH15221.32224.520.5200.1832.34 1.516R11129224.521150.33150.563151R1743.33224.521150.33150.563151R1743.33224.521150.33150.563151R1743.33224.521150.33150.563151R1743.33224.521150.33150.563151R11119.03224.521150.33150.563151表14 分支1立管11供回水立管水力计算表立管总阻力(Pa3943资用压力(Pa4847立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.35224.52 2.2200.1832.34 1.571VG35221.35224.52 3.1150.33150.560467VG45221.35224.52 3.1150.33150.560467VG55221.35224.52 3.1150.33150.560467VG65221.35224.52 3.1150.33150.560467VH15221.35224.520.5200.1832.34 1.516R21129224.521150.33150.563151R2743.33224.521150.33150.563151R2743.33224.521150.33150.563151R2743.33224.521150.33150.563151R2743.33224.521150.33150.563151R21119.03224.521150.33150.563151表15 分支1立管12供回水立管水力计算表立管总阻力(Pa3943资用压力(Pa4805立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.32224.52 2.2200.1832.34 1.571VG25221.32224.52 3.1200.1832.340100VG35221.32224.52 3.1150.33150.560467VG45221.32224.52 3.1150.33150.560467VG55221.32224.52 3.1150.33150.560467VG65221.32224.52 3.1150.33150.560467VH15221.32224.520.5200.1832.34 1.516R11129224.521150.33150.563151R1743.33224.521150.33150.563151R1743.33224.521150.33150.563151R1743.33224.521150.33150.563151R1743.33224.521150.33150.563151R11119.03224.521150.33150.563151表16 分支1立管13供回水立管水力计算表立管总阻力(Pa4310资用压力(Pa4927立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.62224.53 2.2200.1832.34 1.571VG25221.62224.53 3.1150.33150.570467VG35221.62224.53 3.1150.33150.570467VG45221.62224.53 3.1150.33150.570467VG55221.62224.53 3.1150.33150.570467VG65221.62224.53 3.1150.33150.570467VH15221.62224.530.5200.1832.34 1.516R21129224.531150.33150.573151R2743.33224.531150.33150.573151R2743.33224.531150.33150.573151R2743.33224.531150.33150.573151R2743.33224.531150.33150.573151R21119.3224.531150.33150.573151表17 分支1立管14供回水立管水力计算表立管总阻力(Pa4077资用压力(Pa4982立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.2224.51 2.2200.1832.34 1.571VG35221.2224.51 3.1150.33150.550.6467VG45221.2224.51 3.1150.33150.550.6467VG55221.2224.51 3.1150.33150.550.6467VG65221.2224.51 3.1150.33150.550.6467VH15221.2224.510.5200.1832.34 1.516R11129224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R1743.3224.511150.33150.553151R11119224.511150.33150.553151表18 分支1立管15供回水立管水力计算表立管总阻力(Pa4309资用压力(Pa5107立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG15221.2224.51 2.2200.1832.34 1.571VG25221.2224.51 3.1150.33150.550467VG35221.2224.51 3.1150.33150.550467VG45221.2224.51 3.1150.33150.550467VG55221.2224.51 3.1150.33150.550467VG65221.2224.51 3.1150.33150.550467VH15221.2224.510.5200.1832.34 1.516R21129224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R2743.3224.511150.33150.553151R21119224.511150.33150.553151表19 分支1立管16供回水立管水力计算表立管总阻力(Pa4214资用压力(Pa5113立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG112228.51525.83 2.2250.2647.44 1.5104VG212228.51525.83 3.1250.2647.440147VG312228.51525.83 3.1250.2647.440147VG412228.51525.83 3.1250.2647.440147VG512228.51525.83 3.1200.42163.330506VG612228.51525.83 3.1200.42163.330506VH112228.51525.830.5250.2647.44 1.524R12038.09525.831200.42163.333163R12038.09525.831200.42163.333163R12038.09525.831200.42163.333163R12038.09525.831200.42163.333163R12038.09525.831200.42163.333163R12038.09525.831200.42163.333163表20 分支2供回水干管水力计算表编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaBG189572.883851.6332.83500.4967.502216 BG281409.483500.61 5.14500.4556.090.1288 BG373246.073149.58 1.43500.445.730.165 BG467144.32887.2 5.22500.3738.670.1202 BG561042.522624.83 1.33400.56121.210.1161 BG654940.742362.45 5.26400.5198.780.1520 BG748838.962100.08 1.46400.4578.630.1115 BG842737.191837.7 5.23400.3960.770.1318 BG936635.411575.32 1.37320.4491.620.1126 BG1030533.631312.95 5.09320.3764.470.1328 BG1124431.851050.57 1.49320.342.050.163 BG1218330.08788.19 4.99250.39102.950.1514 BG1312228.3525.82 3.01250.2647.440.4143 BH18163.4351.03 5.14200.2875.240.4387BH216326.8702.05 1.43250.3582.410.1118 BH322428.58964.43 5.22320.2735.710.1186 BH428530.361226.81 1.33320.3556.590.175 BH534632.131489.18 5.26320.4282.190.1432 BH640733.911751.56 1.46400.3755.40.181BH746835.692013.93 5.23400.4372.520.1379BH852937.472276.31 1.37400.4991.920.1126BH959039.242538.69 5.09400.54113.590.1578BH1065141.022801.06 1.49500.3636.480.154BH1171242.793063.44 4.99500.3943.350.1216BH1277344.573325.82 3.01500.4350.80.1153BH1389572.883851.6360.16500.4967.50.64061表21 分支2立管1供回水立管水力计算表立管总阻力(Pa2743资用压力(Pa3558立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG18163.4351.03 2.2200.2875.24 1.5166VG28163.4351.03 3.1200.2875.240.6233VG38163.4351.03 3.1200.2875.240.6233VG48163.4351.03 3.1200.2875.240.6233VG58163.4351.03 3.1200.2875.240.6233VG68163.4351.03 3.1200.2875.240.6233VH18163.4351.030.5200.2875.24 1.538R11294351.031200.2875.24375R1908.6351.031200.2875.24375R1908.6351.031200.2875.24375R1908.6351.031200.2875.24375R1908.6351.031200.2875.24375R13235351.031200.2875.24375表22 分支2立管2供回水立管水力计算表立管总阻力(Pa3591资用压力(Pa3661立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG18163.4351.03 2.2200.2875.24 1.5166VG28163.4351.03 3.1200.2875.240.6233VG38163.4351.03 3.1200.2875.240.6233VG48163.4351.03 3.1200.2875.240.6233VG58163.4351.03 3.1200.2875.240.6233VG68163.4351.03 3.1150.51356.2301104VH18163.4351.030.5200.2875.24 1.538R21294351.031200.2875.24375R2908.6351.031200.2875.24375R2908.6351.031200.2875.24375R2908.6351.031200.2875.24375R2908.6351.031200.2875.24375R23235351.031200.2875.24375表23 分支2立管3供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3712立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.77262.38 2.2200.2143.34 1.595VG26101.77262.38 3.1200.2143.340134VG36101.77262.38 3.1200.2143.340134VG46101.77262.38 3.1200.2143.340134VG56101.77262.38 3.1200.2143.340134VG66101.77262.38 3.1200.2143.340134VH16101.77262.380.5200.2143.34 1.522R11252.5262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R11380.88262.381150.38203.033203表24 分支2立管4供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3693立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.78262.38 2.2200.2143.34 1.595VG26101.78262.38 3.1200.2143.340134VG36101.78262.38 3.1200.2143.340134VG46101.78262.38 3.1200.2143.340134VG56101.78262.38 3.1200.2143.340134VG66101.78262.38 3.1200.2143.340134VH16101.78262.380.5200.2143.34 1.522R21252.5262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R21380.88262.381150.38203.033203表25 分支2立管5供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3598立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.77262.38 2.2200.2143.34 1.595VG26101.77262.38 3.1200.2143.340134VG36101.77262.38 3.1200.2143.340134VG46101.77262.38 3.1200.2143.340134VG56101.77262.38 3.1200.2143.340134VG66101.77262.38 3.1200.2143.340134R11252.5262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R11380.88262.381150.38203.033203表26 分支2立管6供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3507立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.78262.38 2.2200.2143.34 1.595VG26101.78262.38 3.1200.2143.340134VG36101.78262.38 3.1200.2143.340134VG46101.78262.38 3.1200.2143.340134VG56101.78262.38 3.1200.2143.340134VG66101.78262.38 3.1200.2143.340134VH16101.78262.380.5200.2143.34 1.522R21252.5262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R21380.88262.381150.38203.033203表27 分支2立管7供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3470立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.77262.38 2.2200.2143.34 1.595VG26101.77262.38 3.1200.2143.340134VG36101.77262.38 3.1200.2143.340134VG46101.77262.38 3.1200.2143.340134VG56101.77262.38 3.1200.2143.340134VG66101.77262.38 3.1200.2143.340134VH16101.77262.380.5200.2143.34 1.522R11252.5262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R11380.88262.381150.38203.033203表28 分支2立管8供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3533立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.78262.38 2.2200.2143.34 1.595VG26101.78262.38 3.1200.2143.340134VG36101.78262.38 3.1200.2143.340134VG46101.78262.38 3.1200.2143.340134VG56101.78262.38 3.1200.2143.340134VG66101.78262.38 3.1200.2143.340134R21252.5262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R21380.88262.381150.38203.033203表29 分支2立管9供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3535立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.77262.38 2.2200.2143.34 1.595VG26101.77262.38 3.1200.2143.340134VG36101.77262.38 3.1200.2143.340134VG46101.77262.38 3.1200.2143.340134VG56101.77262.38 3.1200.2143.340134VG66101.77262.38 3.1200.2143.340134VH16101.77262.380.5200.2143.34 1.522R11252.5262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.033203R11380.88262.381150.38203.033203表30 分支2立管10供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3793立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.78262.38 2.2200.2143.34 1.595VG26101.78262.38 3.1200.2143.340134VG36101.78262.38 3.1200.2143.340134VG46101.78262.38 3.1200.2143.340134VG56101.78262.38 3.1200.2143.340134VG66101.78262.38 3.1200.2143.340134VH16101.78262.380.5200.2143.34 1.522R21252.5262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R21380.88262.381150.38203.033203表31 分支2立管11供回水立管水力计算表立管总阻力(Pa3352资用压力(Pa3786立管不平衡编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.77262.38 2.2200.2143.34 1.595VG26101.77262.38 3.1200.2143.340134VG36101.77262.38 3.1200.2143.340134VG46101.77262.38 3.1200.2143.340134VG56101.77262.38 3.1200.2143.340134VG66101.77262.38 3.1200.2143.340134R11252.5262.381150.38203.033203R1867.1262.381150.38203.033203R1867.1262 .381150.38203.033203R1867.1262.381150.38203.033203R1867.1262.381150.38203.03 3203R11380.88262.381150.38203.033203编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG16101.78262.382.2200.2143.34 1.595VG26101.78262.38 3.1200.2143.340134VG36101.78262.383.1200.2143.340134VG46101.78262.38 3.1200.2143.340134VG56101.78262.383.1200.2143.340134VG66101.78262.383.1200.2143.340134VH16101.78262.380.5200.2143.341.522R21252.5262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.033203R2867.1262.381150.38203.0 33203R21380.88262.381150.38203.033203编号Q(WG(kg/hL(mD(mmυ(m/sR(Pa/mΣξΔPy(PaVG112228.3525.82 2.2250.2647.441.5104VG212228.3525.82 3.1250.2647.440147VG312228.3525.823.1250.2647.440147VG412228.3525.82 3.1250.2647.440147VG512228.3525.823.1250.2647.440147VG612228.3525.823.1250.2647.440147VH112228.3525.820.5250.2647.441.524R12038.05525.821200.42163.323163R12038.05525.821200.42163.323163R12038.05525.821200.42163.323163R12038.05525.821200.42163.323163R12038.05525.82120 0.42163.323163R12038.05525.821200.42163.323163编号负荷(W室温(℃片(mD(mmR22038.831816片20R22038.831817片20R22038.831818片20R22038.831819片20R22038.831821片20R22038.831823片20楼层1四柱760型(无粘砂型楼层4四柱760型(无粘砂型楼层3四柱760型(无粘砂型楼层2四柱760型(无粘砂型层内位置散热器型号楼层6四柱760型(无粘砂型楼层5四柱760型(无粘砂型表33 分支2立管13供回水立管水力计算表立管总阻力(Pa3495本分支最不利立管表34 散热器选型计算表分支1立管1表32 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08080.00% 3206430.00% 8678670.00% 01710.00% 122660.00% 053840.00% 121450.00% 103190.00% 91140.00% 82360.00% 7860.00% 61760.00% 142300.00% 114700.00% 91560.00% 72970.00% 101940.00%73610.00% 54400.00% 84060.00% 371460.00% 01540.00% 01540.00% 01540.00% 01540.00% 01540.00% 37620.00% 2464790.00% 2464790.00% 2464790.00% 2464790.00% 2464790.00% 2464790.00%ΔPj(PaΔP(Pa08080.00% 08080.00% 3206430.00% 13880.00% 8678670.00% 36360.00%ΔPj(PaΔP(Pa01710.00% 122660.00% 102220.00%7910.00%6600.00%152430.00%121580.00%101670.00%81040.00%112110.00%81280.00%61140.00%4590.00%71940.00%31390.00%。