石化年产55万吨对二甲苯项目附录一物料平衡计算书Word文档下载推荐.docx

1、 汇总全流程物料衡算，数据用于完成物料流程图等后续设计任务。1.3.2三苯分离工段物料衡算图1.1三苯分离工段工艺路线图表1.2三苯分离工段总物料衡算inout物流编号REBTXFEEDC7-1C7-2C8C9PRO-BENPFD中编号104105111112114115110物流信息循环混合芳烃混合芳烃甲苯碳八芳烃碳九芳烃精苯产品Temperature C146.125124.6146.4189.086.2Pressure bar1.81.01.41.2Vapor FracEnthalpy Gcal/hr0.604960.667090.882312.728700.10354-0.46563.

2、53635Total Flow kmol/hr237.5851180.85127.667394.832512.824125.797257.320Total Flow kg/hr24129.611367611762.436377.354446.415119.42010.21Total Flow cum/hr32.162131.67415.362347.510572.382721.012024.8866Mass Flow kg/hrC5H10-1C5H12-1BENZENE1860.5718269.87.389522.853220100.2C6H12-1C6H12-2C6H14-1TOLUENE5

3、893.8342202.411751.736344.20.154482.1E-160.00055C7H14-13.0E-099.4E-091.7E-18C7H16-1OX4114.509619.710.032150.0994513728.75.349601.80E-1MX4110.769350.040.518681.6041213458.60.043504.91E-1PX4110.9018315.31.360264.2068322420.60.048572.20E-1C8H10-41.38994831.831.388084.292894827.540.001795.26E-1C8H16-1C8

4、H18-1C9H12-13076.7241.15E-053.55E-059.39E-052.33E-24C9H12-21252.3780.0001240.00038410.734011241.6432.96E-21C9H12-3C9H12-4C9H12-5C9H12-61138.0841679.1412.27E-097.01E-092.94E-162817.2251.29E-33C9H12-71309.7452153.0336.25E-081.93E-076.14E-123462.7784.19E-30C9H12-81589.812925.817.37E-072.28E-061.75E-084

5、515.621.12E-27C10H14-1C10H14-8WATERH2CH4C2H4C2H6C3H6-1C3H8METHANOLTOTAL kg/hr137805.62137805.9表1.3 T101二甲苯塔物料衡算166.8247146.3796188.978Enthalpy kcal/mol0.06852820.2019159-3.701276638.6267512.8306125.79669566.3754447.1215119.2494.9234972.3835721.011814.2632E-130.15487612.1489E-166.0328E-1213734.081372

6、8.735.34985213458.7513458.710.043508622420.9622420.910.04858124827.8794827.8770.00179229.3921E-051252.37710.733961241.6442817.1652.9433E-163462.7156.1354E-124515.5521.74643E-08SULFC4H8-4OX-SMX-SPX-S69566.368表1.4 DWC-101第一三苯分离分隔壁塔物料衡算103C7甲苯产品碳八碳九混合芳烃12086.23632124.63221.51.4162794.028813.743026.9113

7、31418.447257.3201522.513780620100.2148139.41178.281924.8866462.8722520130.6131.6823648096.710.00053078548095.051.24773E-081.7323E-181.24708E-0813734.221.7964E-170.13151613460.784.9059E-152.0249522426.242.2036E-145.2757794833.1195.2554E-145.2403592.3297E-244.76256E-052.9593E-210.0005153211.2879E-339.

8、39796E-094.1891E-302.59106E-071.117E-273.05611E-064.9694E-264.5121E-20137806.212137805.9831.3.3甲苯歧化及烷基转移工段物料衡算图1.2 甲苯歧化及烷基转移工段工艺路线图表1.5甲苯歧化及烷基转移工段总物料衡算GAS-1PRO-BEN2201202203204205217氢气燃气粗苯产品循环芳烃124.6342-4146.06741.0132510.882314-0.465611.03E-05-0.819940.0769810.604961127.6674125.797637.9508935.66352

9、18.14694237.585811762.4515119.4376.504441514.1431314.58824129.6215.3623421.01207929.0317649.91531.54652532.167259.206051181.1791860.57811751.772.14E-165.52E-095.00E-075893.8363.05E-091.02E-221.09E-200.0321585.3496051.11E-165.27E-144114.5060.5186860.0435061.10E-154.15E-134110.7631.3602630.0485781.80E

10、-156.31E-134110.9081.3880880.0017921.92E-185.72E-161.24E-213.59E-187.71E-211.56E-173.16E-205.28E-174.0373250.0005551450.9133.4086Total kg/hr26958.3844426958.351表1.6 T201第一汽提塔物料衡算213歧化反应产物粗苯产物100146.065920.1437583-1.67268-22.990964.2420982.546552291.402635.6631418.14916237.590326958.791514.1251314.74

11、924129.92665.0603649.90841.54671432.167553101.32359.205441181.3241860.7945894.3025.52131E-095.00322E-073.0473E-098.5311E-239.1759E-214114.4971.1078E-165.2664E-144110.7391.0956E-154.1479E-134110.8581.7952E-156.3132E-131.2822681.7673E-185.2818E-161138.0241.2389E-213.5904E-181309.6827.7111E-211.5603E-171589.7423.1634E-205.2843E-174.0379444.0373880.0005555081584.3061450.882133.4246