輸入結(jié)束11—111B1 I*1J輸入數(shù)據(jù)：■項目單位GGGGGGPFG—ngFGFG—ngPG1管線號—7001001700100270010027001007700100770010037001001介質(zhì)HCl1氣體流量kg/h63106744064063078329605102683902氣體密度kg/m31.6396.13； 6.133.23756.1：‘ 17.513.23758.113氣體粘度cp0.014260.011570.011570.011460.011570.0115,7 0.011460.014'4氣體Cp/Cv亠f丄7、r~r^1 1.3341.32641.32641.31731.32641.1) 1.317：1.156-5-初始壓力kPa(a)kPa/100-80~8W-800450800-800-45045016最大允許壓力降IX.1d/丄\J\Jm2020202(2012)2(20管道r1管道長度m10010010010(10C1001001002初選管徑mm40150505(25C200) 15050r3絕對粗糙度mm0.2；0.20.20.2:0.:10.20.:0.2管件Le/D■'145度彎頭15290度彎頭3513180度彎頭754三通（分流）40 「5三通（合流）606閘閥（全開）717截止閥（全開）3008蝶閥（全開）20:19止回閥（全開）13510容器入管口2011其它管件輸出數(shù)據(jù)1最終計算管徑mm3002005080250200200502管道內(nèi)截面積m20.070650.03140.001960.005020.0490630.031L 0.03140.00196213介質(zhì)流速m/s20.577915.4049.374616.9336928.431414.9570828.057186.8066224雷諾數(shù)—41938581632928248443156767:376739245290281585895197228.65流動狀態(tài)一完全湍流完全湍流過渡湍流過渡湍流完全湍流完全湍流完全湍流過渡湍流6摩擦系數(shù)—0.017830.019640.028870.025840.0186110.0196350.0196350.028987管件當量長度m000001()00管道壓降1100m管道壓降kPa9.894167.1224215.51212.540’74 18.39795 19.1812912.64617 11.0062直管段壓降kPa9.894167.1224215.51212.5407418.3979519.1812912.6461711.0068：3局部阻力降kPa000001()004總壓降kPa9.894167.1224215.51212.54074[18.3979519.1812912.6461711.0068：5壓降%%0.899470.89031.939010.56461〔2.2997442.3976612.810262.4459616末端馬赫數(shù)0.04802；0.037190.022750.01625；0.0691350.0649290.066510.02721流量核算流量百米壓降（kPa）40%1.581.142.440.392.943.0'7 2.021.7350% 12.471.783.820.614.604.8() 3.162.7)60%「3.562.565.5(0.886.62； 6.9一 4.553.8970%4.853.497.481.209.019.4()6.2(5.2980%「6.334.569.771.57—11.7r' 12.2：8.096.9.90%8.015.7712.371.9814.90) 15.5,! 10.248.74100%J9.897.1215.272.45P 18.40) 19.1：12.6510.79110%11.978.6218.482.96—22.26i 23.215.3(13.06120%114.2510.2621.993.5226.49) 27.6：118.2115.54130%16.7212.0425.814.1331.09) 32.4：2 21.3718.24140%19.3913.9629.934.7936.06i 37.6() 24.7921.15

150%22.2616.0334.365.5041.4043.1628.4524.28

...輸入結(jié)束■官禺牢TT畀J輸入數(shù)據(jù)：項目單位PG-ng1管線號一7001001PS-ngPSSM-ngSMAN-ngANMMA-ng介質(zhì)1氣體流量kg/h40649147345643(9 6102\ 58681152氣體密度kg/m33.23753.23758.113.2375i 8.1L 3.23758.13.23753氣體粘度cp0.011460.011460.0140.0114()0.01L0.011460.0140.01146'4氣體Cp/Cv1.31731.31731.156「 1.317：J 1.15) 1.31731.156)1.31735初始壓力kPa(a)kPa/1004504504504501 45) 45) 4504506最大允許壓力降IX.1d/丄\J\Jm2() 2() 2()20202()2(120管道1管道長度m10010(10010010()10()1001002初選管徑mm5()2!jj 2!)25 15()100253絕對粗糙度mm0.20.20.20.20..20.220.:i 0.2管件Le/D145度彎頭15——290度彎頭353180度彎頭754三通（分流）405三通（合流）606閘閥（全開）77截止閥（全開）300 8蝶閥（全開）209止回閥（全開）13510容器入管口2011其它管件輸出數(shù)據(jù)1最終計算管徑mm8080508050 200150402管道內(nèi)截面積m20.005024L0.0050240.00196：!0.0050240.0019620.03140.0176620.0012563介質(zhì)流速m/s6.933685)8.3853198.25521]7.7875887.66181316.6736411.37928 7.85594雷諾數(shù)156767189587.7239202.8176073.3222008.6942455.!5989177.188808.95流動狀態(tài)一過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流6摩擦系數(shù)一0.0258380.0256790.0288830.0257380.0289180.0199620.0213390.0314197管件當量長度m0000L000管道壓降1100m管道壓降kPa2.5407373.69308116.136133.19261513.9167〕4.5403097.5505167.9320092直管段壓降kPa2.5407373.69308116.136133.19261513.916714.5403097.5505167.9320093局部阻力降kPa000000004總壓降kPa-2.5407373.69308116.136133.19261513.916714.5403097.5505167.9320095壓降%%0.5646080.8206853.5858060.709473.092603'1.0089581.6778931.7626696末端馬赫數(shù)0.016250.0196770.0331960.018264f0.0307310.0391640.0453120.018523流量核算流量百米壓降（kPa）40%0.390.572.540.492.19—0.71—1.191.2350%0.610.893.970.773.42:1.12\1.8’1.9260%0.881.295.711.114.92:1.612.692.7670%1.201.757.781.516.7(2.19) 3.663.7680%1.572.2910.161.97—8.75「2.86) 4.784.9190%1.982.9012.862.5(11.083.621 6.046.21100%2.453.5815.873.0913.674.477 7.467.67110%2.964.3319.213.7316.555.4() 9.0：‘ 9.281120%3.525.1522.864.4419.696.4：1 10.7411.04130%4.136.0526.835.2123.117.55)12.6112.96140%4.797.0131.116.0526.808.75i 14.6215.03

150%5.508.05I35.726.9430.710.0516.7917.25

...輸入結(jié)束■*z「囂 TL 'Tps|J輸入數(shù)據(jù)： 項目單位FG-CH4LSLSLS1管線號一MMASAR-ngSAR7001001700100270010017001002|7001003介質(zhì)1氣體流量kg/h100153：147579699864612821081002氣體密度kg/m38.113.23758.112.2,78.1-2.377 2.372.373氣體粘度cp0.0140.011460.0140.01180.01L 0.0110.014 0.014'4氣體Cp/Cv亠f丄7、r~r^1 1.1561.31731.156「 1.3247' 1.15() 1.34771.3477[1.3477-5-初始壓力kPa(a)kPa/10045045045045450454506最大允許壓力降IX.1d/丄\J\Jm202()2012\2()2(2020管道1管道長度m10010(10010(10010(10l\1002初選管徑mm258()5020(2F) 15010<p 253絕對粗糙度mm0.20.20.z!0.:0.：:J0.2J0.；i 0.2管件Le/D145度彎頭15—— 290度彎頭353180度彎頭754三通（分流）405三通（合流）606閘閥（全開）7J7截止閥（全開）3008蝶閥（全開）209止回閥（全開）13510容器入管口2011其它管件輸出數(shù)據(jù) 1最終計算管徑mm4010080200200200150402管道內(nèi)截面積m20.0012560.0078510.0050240.03140.03140.03140.0176620.0012563介質(zhì)流速m/s2.72701：1 16.7556110.0558()31.0560210.759722.873813.988399.3316744雷諾數(shù)一63214.29)473544.5466205.:；11953501247091774754.3355348.663214.295流動狀態(tài)一過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流過渡湍流6摩擦系數(shù)一0.0318190.0238090.0252110.0198940.0198840.020030.0217660.0318197管件當量長度m00000000管道壓降1100m管道壓降kPa2.42477710.9373713.0619910.87398:4.7177526.2765393.4010378.2974422直管段壓降kPa2.42477710.9373713.0619910.873984.7177526.2765393.4010378.2974433局部阻力降kPa000000004總壓降kPa-2.42477710.9373713.0619910.873984.7177526.2765393.4010378.2974435壓降%%0.5388392.43052729026642.416441.0483891.3947860.7557861.8438766末端馬赫數(shù)0.0107970.0396420.0402940.061349f0.0427080.0455360.0277580.01862流量核算流量百米壓降（kPa）40%0.371.722.061.72: 0.7￡j 0.980.531.2750%0.582.693.222.68:1.11.540.821.9860%0.833.87—4.643.86i 1.6f2.221.192.8570%1.135.276.315.26i 2.2f3.011.6]3.8880%1.486.898.256.&' 2.9f3.942.1]5.0790%1.878.7110.448.69) 3.7’4.982.676.41100%2.3110.7612.8910.734.6()6.153.297.92110%2.8013.0215.5912.995.6/7.453.999.581120%3.3315.4918.5615.466.7〕8.864.7411.40130%3.9118.1821.7818.14Z.810.405.5713.38140%4.5421.09i 25.2621.049.1：12.066.4615.52

150%5.2124.2129.0024.1510.4813.847.4117.82

輸入結(jié)束■笛遭IT爆汁簽輸入數(shù)據(jù)：項目?單位「LS:LSMS1管線號一700100470010051101介質(zhì)HCl'1氣體流量kg/h208610(3915632氣體密度kg/m32.372.372.371.6393氣體粘度cp0.0140.014 0.0140.01426■4氣體Cp/Cv.-VT-rx/\rr^f. 1.34771.34771.34771.334-5-初始壓力kPa(a)kPa/100450450-806最大允許壓力降IX.1d/丄\J\Jm2C2()2020管道r1管道長度m10010(2001002初選管徑mm1002!5 100403絕對粗糙度mm0.2:0.20.:!0.2管件Le/D145度彎頭15290度彎頭35131