设计院物料平工程名60万吨醇物料平工程名

衡表称氨衡表称

设计工全厂物料平衡表设计工全厂物料平衡表

程程

文件编版次0文件编版次0

号号

编制校核审核日期页码编制校核审核日期页码

2022-11-2022-11-

33

物料号〈1〉 〈2〉 〈3〉〈4〉〈5〉〈6〉〈7〉〈8〉〈9〉〈10〉〈11〉

物料名原料煤氧气水煤气变换气净化气配氮气液氮洗合成气液氨硫磺燃料气

称富氢气

组 分分子式分子量〔w〕%m3(标)/hm3(标)/hm3(标)/hm3(标)/hm3(标)/hm3(标)/hm3(标)/hm3(标)/h

(V)%(V)%(V)%(V)%(V)%(V)%(V)%t/ht/h(V)%

一氧化98123.2065.2101972.980.802022.891.3953.632.921953.25 15.76

CO28

氢气35120.3123.340131277.93 91.211320.1171.87171.96 1.39

H22131270.53 53.23129785.86 75.00

二氧化4870.803.237101021.01 40.9615.700.010.0020.000115.70 0.13

CO244

甲烷3.760.0033.760.0023.760.00260.013.75 0.03

CH4160.0006

氩气177.900.40172.820.115172.820.07172.820.123.510.19169.31 1.37

Ar40

氮气10455.826.94910455.824.2410455.827.2633294.17 99.99459.5725.0243261.9525.00 28.47 81.33

N228

硫化氢总硫1543.101.0261701.200.69

H2S343.50<0.1ppm

氧硫化176.050.1178.80

COS605.5ppm

NH317

氧气44296.7399.600.01

O2323.33

干基∑44474.63 100.00150472.63 100.00246606.92 100.00143932.91 100.0033297.50 100.001836.80100.00173047.81 100.0063.162442.428212393.7367100.00

90.87

温度℃40.00216.035

40.0030.0040.0030.0040.00

压力6.003.71.300.18

MPa(A)3.503.203.753.00