输入数据:项目单位GGGGGGFG-ngFGFG-ngPG1管线号-7001001 7001002 7001002 7001007700100770010037001001介质HCl1气体流量kg/h63106744064063078329605102683902气体密度kg/m31.6396.136.133.23756.1317.513.23758.113气体粘度cp0.01426 0.01157 0.01157 0.011460.011570.011570.011460.0144气体Cp/Cv-1.3341.32641.32641.31731.32641.191.31731.1565初始压力kPa(a)808008004508008004504506 最大允许压力降kPa/100m2020202020202020管道1管道长度m1001001001001001001001002初选管径mm401505050250200150503绝对粗糙度mm0.20.20.20.20.20.20.20.2管件Le/D145度弯头15290度弯头353180度弯头754三通（分流）405三通（合流）606闸阀（全开）77截止阀（全开）3008蝶阀（全开）209止回阀（全开）13510容器入管口2011其它管件输出数据1最终计算管径m m3002005080250200200502管道内截面积m20.070650.0314 0.00196 0.00502 0.0490630.03140.0314 0.0019623介质流速m/s20.577915.404 9.37461 6.9336928.4314 14.95708 28.05718 6.8066224雷诺数-4193858 1632928248443156767376739245290281585895 197228.65流动状态-完全湍流完全湍流过渡湍流过渡湍流 完全湍流完全湍流完全湍流过渡湍流6摩擦系数-0.01783 0.01964 0.02887 0.02584 0.018611 0.019635 0.0196350.028987管件当量长度m00000000 管道压降1100m管道压降kPa9.89416 7.12242 15.5121 2.54074 18.39795 19.18129 12.64617 11.006832直管段压降kPa9.89416 7.12242 15.5121 2.54074 18.39795 19.18129 12.64617 11.006833局部阻力降kPa000000004总压降kPa9.89416 7.12242 15.5121 2.54074 18.39795 19.18129 12.64617 11.006835压降%%0.899470.8903 1.93901 0.56461 2.299744 2.3976612.81026 2.4459616末端马赫数0.04802 0.03719 0.02275 0.01625 0.069135 0.0649290.066510.02721流量核算流量百米压降(kPa)40%1.581.142.440.392.943.072.021.7350%2.471.783.820.614.604.803.162.7060%3.562.565.500.886.626.914.553.8970%4.853.497.481.209.019.406.205.2980%6.334.569.771.5711.7712.288.096.9190%8.015.7712.371.9814.9015.5410.248.74100%9.897.1215.272.4518.4019.1812.6510.79110%11.978.6218.482.9622.2623.2115.3013.06120%14.2510.2621.993.5226.4927.6218.2115.54130%16.7212.0425.814.1331.0932.4221.3718.24140%19.3913.96...
