最不利环路水力计算表

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1、最不利环路水力计算表管段流量管段尺寸(BxH)长度(m)ν(m/s)R(Pa/m)△Py(Pa)ξ动压(Pa)△Pj(Pa)管段阻力(Pa)1-20.1225012034.001.4404.3191.389.6013.2517.572-30.2425025033.840.7792.3371.588.8514.0116.353-40.4850025083.840.5464.3690.308.852.657.024-50.9663025086.101.1869.4870.3022.296.6916.175-61.4463032087.141.29910.3890.3030.619.1819.57

2、6-71.9280032087.501.30110.4080.3033.7510.1220.537-82.1680040086.750.8847.0690.5027.3313.6720.748-92.4080040037.501.0793.2360.5033.7516.8720.11送风支管水力计算结果管段流量管段尺寸(BxH)长度(m)ν(m/s)R(Pa/m)△Py(Pa)ξ动压(Pa)△Pj(Pa)管段阻力(Pa)10-110.1225012034.001.4404.3191.389.6013.2517.5711-40.2425025033.840.7792.3371.488.8513

3、.0915.4312-130.1225012034.001.4404.3191.389.6013.2517.5713-50.2425025033.840.7792.3371.488.8513.0915.4314-150.1225012034.001.4404.3191.389.6013.2517.5715-60.2425025033.840.7792.3371.488.8513.0915.4316-170.1225012034.001.4404.3191.389.6013.2517.5717-70.2425025033.840.7792.3372.788.8524.5926.9318-190

4、.1225012034.001.4404.3191.389.6013.2517.5719-80.2425025033.840.7792.3372.788.8524.5926.9320-210.1225012034.001.4404.3191.389.6013.2517.5721-220.2425025033.840.7792.3372.788.8524.5926.9323-240.1225012034.001.4404.3191.389.6013.2517.5724-250.2425025033.840.7792.3371.678.8514.7717.1126-270.1225012034.

5、001.4404.3191.389.6013.2517.5727-30.2425025033.840.7792.3371.588.8514.0116.3528-290.1225012034.001.4404.3191.389.6013.2517.5729-40.2425025033.840.7792.3371.488.8513.0915.4330-310.1225012034.001.4404.3191.389.6013.2517.5731-50.2425025033.840.7792.3371.488.8513.0915.4332-330.1225012034.001.4404.3191.

6、389.6013.2517.5733-60.2425025033.840.7792.3371.488.8513.0915.43回风管水力计算结果管段流量管段尺寸长度(m)ν(m/s)R(Pa/m)△Py(Pa)ξ动压(Pa)△Pj(Pa)管段阻力(Pa)34-350.50500250164.000.5899.4250.99.608.6418.0635-361.00630320164.960.65410.4650.914.7613.2923.7536-371.5080032037.75.860.81630.7801.5620.6032.1362.9137-382.001000320166.25

7、0.85813.7300.923.4421.0934.8238-392.481000400266.200.69217.9952.3623.0654.4372.42部件ξ散流器1.28渐扩管0.1渐缩管0.1散流器1.28渐扩管0.1分流三通1.5分流四通0.290度弯头0.39渐缩管0.1渐扩管0.1回风口0.8