输入结束
1123456
输入数据项目管线号介质气体流量
单位HClkgh
3
GGGGGGFG
g7001001700100270010027001007631067440640630783613001157132648002010025002
FG70010072960517510011571198002010020002
FG
g70010031026832375001146131734502010015002
PG700100139081100141156450201005002
气体密度气体粘度气体CpCv初始压力最大允许压力降管道1管道长度2初选管径3绝对粗糙度管件145度弯头290度弯头3180度弯头4三通（分流）5三通（合流）6闸阀（全开）7截止阀（全开）8蝶阀（全开）9止回阀（全开）10容器入管口11其它管件输出数据
kgm163961361332375cp0014260011570011570011461334132641326413173kPaa80800800450kPa100m20202020mmmmmLeD15357540607300201352010040021001500210050021005002
1最终计算管径
234567123456管道内截面积介质流速雷诺数流动状态摩擦系数管件当量长度管道压降100m管道压降直管段压降局部阻力降总压降压降末端马赫数流量核算百米压降kPa
mm
m2msmkPakPakPakPa流量405060708090100110120130140150
300
200
50
80
250
200
200
50
000196268066221972286过渡湍流0028980
0070650031400019600050200490630031400314205779154049374616933692843141495708280571841938581632928248443156767376739245290281585895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001783001964002887002584001861100196350019635000000098941698941609894160899470048021582473564856338019891197142516721939222671224271224207122420890300371911417825634945657771286210261204139616031of4155121155121015512119390100227524438255074897712371527184821992581299334362540742540740254074056461001625039061088120157198245296352413479550183981839795018397952299744006913529446066290111771490184022262649310936064140
191813126462110068191812912646171100683000191812912646171100683239766128102624459610064929006651002721307480691940122815541918232127623242376043162023164556208091024126515301821213724792845173270389529691874107913061554182421152428
D制苯C00012管线表计算256682466xlsGas_Pipe
20153302027
f输入结束
1123456
输入数据项目管线号介质气体流量
单位kgh
3
PG
g7001001406
PS
g4913237500114613173450201002502
PS47381100141156450201002502
SM
g4563237500114613173450201002502
SM43981100141156450201002502
AN
g61023r