附表 水力计算

附表2区域一风管最不不利环路水水力计算表表（假定流流速法）编号风量(m^3/h)风速(m/s)Rm(Pa/m)宽(mm)高(mm)长(m)ζ△Pd(Pa)△Pl(Pa)△P(Pa)管段165400.00014.531.581250.0001000.0005.150.000.008.138.13管段2921.134.261.30500.00120.001.501.0816.781.9518.73管段329476.0068.190.611250.000800.006.300.9538.353.8742.23管段414738.0038.190.971000.000500.006.301.0542.246.1348.36管段514738.0038.190.971000.000500.001.700.2710.711.6512.37管段613816.9907.680.861000.000500.003.400.000.052.932.97管段712895.7777.160.751000.000500.003.400.000.052.572.61管段811053.5527.680.95800.00500.003.400.000.003.223.22管段99211.2778.001.22800.00400.003.400.000.004.144.14管段107369.0118.001.47800.00320.003.400.000.005.005.00管段115526.7667.621.47630.00320.003.400.000.034.995.02管段123684.5118.002.00400.00320.003.400.000.006.796.79管段131842.2558.193.22250.00250.003.400.000.0010.9510.95管段14921.134.090.88250.00250.001.800.7912.921.5814.50当前最不利环路的阻力损失为179.78Pa。附表3区域二风管最不不利环路水水力计算表表（假定流流速法）编号风量(m^3/h)风速(m/s)Rm(Pa/m)宽(mm)高(mm)长(m)ζ△Pd(Pa)△Pl(Pa)P(Pa)管段165400.0009.080.481600.0001250.0002.700.000.001.311.31管段265400.0009.080.481600.0001250.0000.300.000.000.150.15管段359873.2248.320.411600.0001250.0000.300.000.100.120.23管段459873.2248.320.411600.0001250.0001.500.000.000.610.61管段559873.2248.320.411600.0001250.0001.200.000.000.490.49管段646056.3348.000.441600.0001000.0006.900.000.023.073.09管段730397.1186.750.361250.0001000.0008.400.010.233.073.30管段813816.9907.680.861000.000500.007.201.1540.736.2046.92管段913816.9907.680.861000.000500.002.700.279.412.3211.74管段1012895.7777.160.751000.000500.004.000.000.053.023.07管段1111974.6658.321.10800.00500.004.000.000.004.414.41管段1211053.5527.680.95800.00500.004.000.000.073.793.87管段139211.2778.001.22800.00400.004.000.000.004.874.87管段147369.0118.001.47800.00320.004.000.000.005.885.88管段155526.7667.621.47630.00320.004.000.000.035.875.90管段163684.5118.002.00400.00320.004.000.000.007.997.99管段171842.2558.193.22250.00250.004.000.000.0012.8912.89管段18921.134.090.88250.00250.002.700.7912.922.3715.29当前最不利环路的阻力损失为131.99Pa。附表4区域三风管最不不利环路水水力计算表表（假定流流速法）编号风量(m^3/h)风速(m/s)Rm(Pa/m)宽(mm)高(mm)长(m)ζ△Pd(Pa)△Pl(Pa)P(Pa)管段165400.0009.080.481600.0001250.0003.000.000.001.451.45管段254346.4487.550.341600.0001250.0005.400.010.341.842.18管段348819.7726.780.281600.0001250.0007.200.000.102.002.10管段437766.2208.200.551600.000800.004.500.000.002.492.49管段532239.4447.000.411600.000800.007.200.010.222.953.17管段621185.9927.360.561000.000800.009.000.000.005.055.05管段711053.5527.680.95800.00500.008.100.000.007.687.68管段89211.2778.001.22800.00400.001.801.0841.422.1943.61管段97369.0118.001.47800.00320.003.900.000.005.735.73管段105526.7667.621.47630.00320.003.900.000.035.725.75管段113684.5118.002.00400.00320.003.900.000.007.797.79管段121842.2558.193.22250.00250.003.900.000.0012.5612.56管段13921.134.090.88250.00250.002.100.7912.921.8414.76当前最不利环路的阻力损失为117.57Pa。附表5区域四风管最不不利环路水水力计算表表（假定流流速法）编号风量(m^3/h)风速(m/s)Rm(Pa/m)宽(mm)高(mm)长(m)ζ△Pd(Pa)△Pl(Pa)P(Pa)管段165400.00014.531.581250.0001000.0006.550.000.0010.3510.35管段254346.44812.081.111250.0001000.0006.600.010.877.308.17管段340529.5589.010.631250.0001000.0006.600.021.104.165.26管段424870.4426.910.451250.000800.003.300.020.541.472.01管段517501.4417.600.68800.00800.007.200.000.004.874.87管段617501.4417.600.68800.00800.002.400.248.311.629.93管段715659.1156.800.55800.00800.003.400.000.111.861.97管段813816.9907.620.79800.00630.003.400.000.002.692.69管段911974.6658.321.10800.00500.003.400.000.003.753.75管段1010132.3397.040.80800.00500.003.400.010.252.732.98管段118290.1447.201.00800.00400.003.400.000.003.393.39管段126447.8997.111.08630.00400.003.400.000.003.683.68管段134605.6338.001.73400.00400.003.400.00