第1页，共7页管径计算表热负荷WKg/h127186.00935.2041.0010.0016.19161.910.2019.032.5047.57209.48247338.001628.4353.0032.0012.70406.290.2120.664.0082.65488.94359594.002050.0353.004.0019.6578.610.2632.751.0032.75111.36479430.002732.3953.0012.0034.05408.560.3458.174.00232.69641.255183968.006328.5080.505.0020.35101.730.3558.642.00117.27219.00183969.006328.5380.505.0020.35101.730.3558.642.00117.27219.00679430.002732.3953.003.5034.05119.160.3458.176.00349.04468.20747971.001650.2053.0033.0013.02429.650.2121.222.0042.44472.08835715.001228.6041.0020.0027.16543.270.2632.843.50114.95658.223487.536a31459.001082.1941.004.5021.3496.040.2325.484.00101.92197.9715563535.3721.250.00156.220.000.4286.420.000.000.0015563535.3727.0066.0046.213049.800.2633.1680.502669.225719.025719.029206.5520152693.2327.0026.0075.741969.210.3455.6046.502585.184554.3920152693.2335.7537.0018.32677.770.1918.0929.00524.551202.325756.71管段管径dmm管长Lm单位摩阻RPa/m摩损RxLPa速度Vm/s动压头hwPa局部阻力系数局部阻力损失Z=hw(pa)总阻力RL+ZPa（一）环路最不利环路阻力损失平衡阻力=5928K=(5756-5928)/5928=-3.0%≤15%（满足要求）（二）环路平衡阻力=6607第2页，共7页11623399.8321.2517.0089.111514.790.3148.2033.501614.743129.5211623399.8327.0060.0026.571594.130.1918.4986.001590.513184.646314.1612256421.6121.2517.0098.641676.870.3353.5930.001607.833284.7012256421.6127.0070.0029.372055.740.2020.5679.001624.523680.266964.9619836682.3621.250.00249.920.000.53140.390.000.000.0019836682.3627.0057.0073.484188.140.3353.8768.003662.847850.987850.98928995.00997.4335.7531.0036.531132.510.2837.453.00112.341244.841051569.001773.9753.003.0014.9344.790.2224.523.5085.82130.6111104538.003596.1153.005.0057.82289.080.45100.763.00302.29591.37104539.003596.1453.005.0057.82289.080.45100.765.50554.21843.291285421.002938.4853.002.0039.1678.310.3767.283.50235.48313.791372899.002507.7353.0016.0028.88462.080.3249.002.50122.50584.581450325.001731.1853.005.0014.2671.280.2223.351.5035.03106.301528995.00997.4341.0023.0018.29420.610.2121.655.50119.05539.66435...
