精品环氧乙烷工段工艺流程图物料流程图物料衡算表文档格式.docx

1、ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO30.0000.0050.19599.80.05099.850.1002.00196.900.4930.6060.0130.5341.1663.4515.63853.3828.641.8455.3370.5371.1554.0435.02852.1428.661.9786.4440.0120.5001.0953.2398.32050.1030.001.7315.0011.0773.7728.15148.641.8466.0012.5760.0011.6971.1093.2815.35950.7427.221.7546.254

2、1.9881.0913.8204.75049.2727.081.8697.559温度（）40301078.8779.7775.6776.28134.18136.09压力（MPa）2.752.551.761.47质量流量（Kg/Hr）7622.18703.86961.67276.9119.6113.7169330171019184033187113184031187111摩尔流量（Kmol/Hr）238.1271.9248.1259.47.256.887326.47281.77819.97720.9体积流量（M3/Hr）222.2253.8207.4216.86.316.001185511809

3、12526.712546.217439.817555.3密度（kg/m3）34.333.618.914.314.514.714.910.610.7表二：二氧化碳部分201203204205206工艺放空CO2吸收塔进料CO2吸收塔顶部物料V201罐底部物料P202出口液相0.5301.1523.4085.56752.71028.2891.8226.5090.5321.1363.9804.94951.32428.2211.9477.8977.7521.1203.3125.41051.22827.4611.7701.9347.5771.1233.9304.88750.68527.8281.9232

4、.034100.0093.4572.2401.8012.50238.01538.2861.75461.937111501.4251.4221.8251.7901.780.147318.5317.247584.746945.746215.244354.02733.62539.4303965.4370438.113.62713.32036.21972.12093.51995.2151.7141.013090.315953.023.84323.3512995.02901.13667.93520.22.7702.573265.472323.5密度（kg/m3）13.413.615.916.212.69

5、871145表三：二氧化碳系统部分207208/309209210213C201到C202进料V202顶部闪蒸汽V202到C202进料C202顶部放空C203底部物料0.00292.6822.2470.0060.0091.0723.9810.0556.7270.2841.5622.43321.74631.4880.82234.8840.0457.7140.2451.5911.90418.55127.7660.77741.40792.7872.2231.0683.91984.2390.0440.02515.6850.00082.2250.0460.02617.6961.25197.6360.96

6、00.0600.0160.0280.0401.25097.6220.9660.049636410441.81141.9911.8000.3150.3210.1271.4501.447307368.9374967.7104.6151.1310000.8377356.112795.014475.229500013044.315913.13.4154.73013193.616060.1578.6639.815663.815659.5266.120324.64729.99441.657268.399326.713983.615819.9298.311553.53.60.915989.988.8表四：环

7、氧吸收部分214215216217/308218C205进料C204到V301进料C203到V204进料K301入口物料P206入口物料1.25996.8601.6310.0380.1641.21597.3131.2560.0150.12638.8720.01158.5510.0140.0310.4660.8010.0191.18339.0030.02258.2080.0360.0410.4490.7900.0201.4120.3031.9660.2201.2861.94219.0490.75942.9880.4461.9670.2001.3761.58916.97228.6240.74248

8、.08398.9610.9740.06198.9540.98046.6547.8105.0104.935.3155.4155.9123.71.461.4520.2051.571.5671403.41792.315871.16039.9173751176467571.9674.830748630741773.194.4556.1560.17434.47412.917.519.916619.916613.31.4141.8118326.88383.512912.712894.638.844.4327.1992.8989.81.913.715.2939.9表五：环氧吸收解析部分219220/415221222223224/319C203到C204进料P210到C406C205到C206C203贫液进料C303/304贫液进料塔釜出料1.32997.60.9590.0391.34297.5360.9650.04780.92217.8181.1670.09480.92317.8170.09398.3721.4290.000.0.1440.05398.7331.1030.11198.960.