1、设计院物料平衡表工程名称60万吨醇氨物料平衡表-工程名称一设计项目全厂物料平衡表一设计项目.全厂物料平衡表文件编号版次0一文件编号.版次0编制校核审核日期页码编制校核审核日期页码物料号(8)(10)物料名称原料煤氧气水煤气变换气净化气配氮气液氮洗富氢气合成气液氨硫磺燃料气组分分子式分子量(w)%m3(标)h(V)%m3(标)h(V)%m3(标)h(V)%m3(标)h(V)%m3(标)h(V)%m3(标)h(V)%m3(标)h(V)%ththm3(标)h(V)%氧化碳CO2898123.2065.2101972.980.802006.891.3953.632.921953.2515.76氢气H2
2、235120.3123.340131270.5353.23131277.9391.211320.1171.87129785.8675.00171.961.39氧化碳CO2444870.803.237101021.0140.9615.700.010.0020.000115.700.13甲烷CH4163.760.0033.760.0023.760.00260.010.00063.750.03气Ar40177.900.40172.820.115172.820.07172.820.123.510.19169.311.37氮气N22810455.826.94910455.824.2410455.827.
3、2633294.1799.99459.5725.0243261.9525.0028.4781.33硫化氢H2S34总硫3.501543.101.0261701.200.690.1ppm氧硫化碳60176.050.1178.805.5ppm氨NH317氧气023244296.7399.603.330.01干基90.8744474.63100.00150472.63100.00246606.92100.00143932.91100.0033297.50100.001836.80100.00173047.81100.0063.162442.428212393.7367100.00温度40.00216.040.0030.0040.0030.0040.0035压力MPa（八）6.003.73.503.203.751.303.000.18
