液体甲烷含量：xCH4LCH4L00004720975409x100％0048％出口液体氩含量：xArLArL00000390975409x100％0004％出口液体氢气含量：xH2LH2L00003280975409x100％00336％出口液体氮气含量：xN2LN2L00001380975409x100％00141％液氨贮槽出口液氨组分（％）NH3998998CH40048Ar0004H200336N200141小计10000
出口弛放气组分含量：弛放气氨含量：yNH3M0NH3LNH3V0989620974430024591x100％61784％弛放气甲烷含量：yCH4M0CH4LCH4V0002480000472002459x100％815％弛放气氩含量：yArM0ArLArV00005700000390024591x100％215％弛放气氢气含量：yH2M0H2LH2V000505200003280024591x100％1921％弛放气氮气含量：yN2M0N2LN2V000227700001380024591x100％8698％出口弛放气组分含量NH361784CH4815Ar215H21921N28698小计10000
137液氨贮槽物料计算：以液氨贮槽出口一吨纯液氨为基准折标立方米计算液氨贮槽出口液体量３L191000x2240998998x171318969m３其中NH3L19NH3L19NH3xX19NH31318969x9989981317647m３CH4L19CH4L19CH4xX19CH41318969x004840638m３ArL19ArL19ArxX19Ar1318969x00040053m３H2L19H2L19H2xX19H21318969x003360053m３N2L19N2L19N2xX19N21318969x001410186m液氨贮槽出口弛放气（VL）0025３V200025xL190025x131896932974m３其中NH3V20NH3V20NH3×y20NH332974x6187420373m３CH4V20CH4V20CH4×y20CH432974x81492687m３ArV20ArV20Ar×y20Ar32974x21590712m３H2V20H2V20H2×y20H232974x19216334m３N2V20N2V20N2×y20N232974x86982868m
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f化工课程设计
液氨贮槽出口总物料L19V201318969329741351943m液氨贮槽进口液体：３由物料平衡，入槽总物料出槽总物料，L21L19V201351943m入口液体各组分含量计算L21iL19iV20i３其中NH3L21NH31317647203731338020m３CH4L21CH4063826873325m３ArL21Ar005307120765m３H2L21H2044363346777m３N2L21N2018628683054m入口液体中组分含量核算由m0iL21iL21入口液体中氨含量m0NH31338021351943x1009897入口液体中甲烷含量m0CH433251351943x1000246入口液体中氩含量m0Ar07651351943x1000057入口液体中氢气含量m0H267771351943x1000501入口液体中氮气含量m0N230451351943x1000226入口液体中组分含量m0i≈M0i138合成系统物料计算将整个合成看着一个系统，进入该系统的物料有新鲜补充气补V补，离开该系统的物料有r