附录2-物料衡算一览表

物料衡算一览表2018年“东华科技-陕鼓杯”第十二届全国大学生化工设计竞赛兰州石化5万吨/年甲基丙烯酸甲酯项目物料衡算一览表团队名称： 府学路18号团队 团队成员：陈弘男 曾辉 陈钊宜 要馨惠 晏燕指导老师：黄星亮 孟祥海 王成秀 杜巍 徐建2018年8月目录第一章 总论1第二章 物料衡算原理2第三章 物料衡算任务3第四章 物料衡算44.1 异丁烯提纯工段44.1.1 R0101异丁烯水合预平衡反应器54.1.2 T0101异丁烯水合反应精馏塔54.1.3 T0102叔丁醇分水塔64.1.4 R0102叔丁醇脱水预平衡反应器84.1.5 T0103叔丁醇脱水反应精馏塔94.2 甲基丙烯醛合成工段104.2.1 R0201甲基丙烯醛合成反应器114.2.2 T0201急冷吸收塔134.2.3 V0201气液分离罐144.2.4 T0202共沸精馏塔154.2.5 T0203甲醇回收塔164.2.6 T0204甲醇-水精馏塔174.2.7 T0205甲醇-水精馏塔184.3 甲基丙烯酸甲酯合成工段204.3.1 R0301甲基丙烯酸甲酯合成反应器224.3.2 V0301气液分离罐234.3.3 T0301甲醇回收塔244.3.4 T0303双溶剂萃取塔254.3.5 T0303甲基丙烯酸甲酯产品精制塔264.3.6 T0304萃取剂回收塔274.3.7 T0305分水塔284.3.8 T0306甲基丙烯醛回收塔294.4 全流程物料衡算30府学路18号团队 第一章 总论本项目以甘肃省兰州市中国石化分公司抽余碳四为原料，经异丁烯提纯工段后，高纯异丁烯气体进入甲基丙烯醛合成反应器，反应产物通过甲醇急冷喷淋、精馏等手段将甲基丙烯醛分离出来，再将甲基丙烯醛与甲醇通入甲基丙烯酸甲酯合成反应器，通过吸收、双溶剂萃取以及精馏等手段将甲基丙烯酸甲酯产品分离出来，得到优等品甲基丙烯酸甲酯。在已确定化学生产工艺和流程后，由定性阶段转向定量阶段，通过对整个生产系统、生产车间，以及部分重要的生产单元进行物料衡算计算出主、副产品的产量，原材料的消耗定额、“三废”排放量及组成，以及产品收率等各项经济技术指标，从而定量地评述初步设计所选择的工艺路线、生产方法及工艺流程在经济上是否合理，技术上是否先进，为后阶段的设计提供数据。第二章 物料衡算原理系统累计的质量输入系统的质量输出系统的质量反应生成的质量反应消耗的质量假设系统无泄漏，有：dFdt=FIN-FOUT+GR-CR当系统无化学反应发生时，有：dFdt=FIN-FOUT 在稳定状态下，有：dFdt=FIN-FOUT=0，FIN=FOUT注：FIN进入系统的物料流率；FOUT流出系统的物料流率；GR反应产生物料速率；CR反应消耗物料速率。第三章 物料衡算任务对于本厂，工艺年开工以甲基丙烯酸甲酯合成装置325天/年（8000小时）为准的连续操作，其中一年内的五六周（约40天）用于固定的停车设备检修及紧急情况处理。物料衡算的主要任务在于：确定产品甲基丙烯酸甲酯的产量以及质量指标；确定吸收液、甲醇、甲基丙烯醛循环量以及损失率等指标；确定工艺中的“三废”排放量等公共经济指标；各主要单元过程的物料衡算，并指导工艺设备的尺寸确定；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 第四章 物料衡算4.1 异丁烯提纯工段图4-1 异丁烯提纯工段工艺流程简图图4-2 异丁烯提纯工段工艺流程简图本工段主要有异丁烯水合预平衡反应器、异丁烯水合反应精馏塔、叔丁醇分水塔、叔丁醇脱水预平衡反应器以及叔丁醇脱水反应精馏塔。主要设备物料衡算如下。4.1.1 R0101异丁烯水合预平衡反应器表4-1 异丁烯水合预平衡反应器R0101进出口物流表进出口inout物流编号S102S103Mass Flow kg/hrISOC4H84190.05201704.1490H2O30000.000029201.8140C3H613.689013.6890C3H82.28202.2820NC4H10857.8600857.860ISOC4H10230.4360230.43601C4H83793.06403793.0640CISC4H81123.66001123.6600TRANC4H81176.13501176.135013C4H67.98507.9850NC5H123.42203.4220ISOC5H129.12609.1260TBA3.955210-113284.0900Total Flow kmol/hr1867.94701823.6410Total Flow kg/hr41407.712041407.7120Total Flow l/min834.2970826.4190Temperature C70.000070.0000Pressure atm4.93504.9350Vapor Frac0.00000.0000Liquid Frac1.00001.0000Enthalpy cal/sec-113.875-114.3314.1.2 T0101异丁烯水合反应精馏塔 表4-2 异丁烯水合反应精馏塔T0101进出口物流表进出口inout物流编号H2O-1S103S104S105Mass Flow kg/hrISOC4H80.00001704.1490188.02380H2O5000.000029201.81000.130733714.88MAL0.00000.00000.00000.0000O20.00000.00000.00000.0000N20.00000.00000.00000.0000CH4O0.00000.00000.00000.0000MMA0.00000.00000.00000.0000N-HEX-010.00000.00000.00000.0000C3H60.000013.689313.68931.68145E-08C3H80.00002.28152.28158.75626E-08NC4H100.0000857.8599854.02963.8302ISOC4H100.0000230.4358230.35570.08011C4H80.00003793.06403792.79300.2710CISC4H80.00001123.66001122.50501.1551TRANC4H80.00001176.13501175.65800.477513C4H60.00007.98547.98544.173610-27NC5H120.00003.42233.42230.0000ISOC5H120.00009.12629.12621.401810-28TBA0.00003284.09000.00045287.0190CO0.00000.00000.00000.0000CO20.00000.00000.00000.0000MAA0.00000.00000.00000.0000HQ0.00000.00000.00000.0000Total Flow kmol/hr277.54221823.641131.27221942.889Total Flow kg/hr5000.000041407.71007400.000039007.7100Total Flow l/min83.8400826.4190218.6534775.0131Temperature 25.000070.000045.8393136.9551Pressure atm4.9346164.9346164.93465.0215Vapor Frac0.00000.00000.00000.0000Liquid Frac1.00001.00001.00001.0000Enthalpy Gcal/hr-18.9453-114.3313-1.2580-129.11114.1.3 T0102叔丁醇分水塔表4-3 叔丁醇分水塔T0102进出口物流表进出口inout物流编号S107S108S112Mass Flow kg/hrISOC4H80.0000 0.0000 0.0000 H2O37654.3800 2664.3810 34990.0000 MAL0.0000 0.0000 0.0000 O20.0000 0.0000 0.0000 N20.0000 0.0000 0.0000 CH4O0.0000 0.0000 0.0000 MMA0.0000 0.0000 0.0000 N-HEX-010.0000 0.0000 0.0000 C3H60.0000 0.0000 0.0000 C3H80.0000 0.0000 0.0000 NC4H103.8305 3.8305 0.0000 ISOC4H100.0801 0.0801 0.0000 1C4H80.2710 0.2710 0.0000 CISC4H81.1551 1.1551 0.0000 TRANC4H80.4776 0.4776 0.0000 13C4H60.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 TBA5365.2280 5365.2280 0.0000 CO0.0000 0.0000 0.0000 CO20.0000 0.0000 0.0000 MAA0.0000 0.0000 0.0000 HQ0.0000 0.0000 0.0000 Total Flow kmol/hr2162.6200 220.3798 1942.2400 Total Flow kg/hr43025.4200 8035.4230 34990.0000 Total Flow l/min789.5515 169.4098 635.5666 Temperature 80.0632 80.5524 100.6960 Pressure atm3.4878 0.9869 1.0244 Vapor Frac0.0000 0.0000 0.0000 Liquid Frac1.0000 1.0000 1.0000 Enthalpy Gcal/hr-146.5730 -15.8523 -129.8819 4.1.4 R0102叔丁醇脱水预平衡反应器表4-4 叔丁醇脱水预平衡反应器R0102进出口物流表进出口inout物流编号S109S110Mass Flow kg/hrISOC4H80.0000 1000.9790 H2O2664.3810 2985.7800 MAL0.0000 0.0000 O20.0000 0.0000 N20.0000 0.0000 CH4O0.0000 0.0000 MMA0.0000 0.0000 N-HEX-010.0000 0.0000 C3H60.0000 0.0000 C3H80.0000 0.0000 NC4H103.8305 3.8305 ISOC4H100.0801 0.0801 1C4H80.2710 0.2710 CISC4H81.1551 1.1551 TRANC4H80.4776 0.4776 13C4H60.0000 0.0000 NC5H120.0000 0.0000 ISOC5H120.0000 0.0000 TBA5365.2280 4042.8490 CO0.0000 0.0000 CO20.0000 0.0000 MAA0.0000 0.0000 HQ0.0000 0.0000 Total Flow kmol/hr220.3798 238.2202 Total Flow kg/hr8035.4230 8035.4230 Total Flow l/min166.4375 170.8007 Temperature C70.0000 70.0000 Pressure atm0.9869 0.9869 Vapor Frac0.0000 0.0000 Liquid Frac1.0000 1.0000 Enthalpy cal/sec-15.9609 -15.7956 4.1.5 T0103叔丁醇脱水反应精馏塔表4-5 叔丁醇脱水反应精馏塔T0103进出口物流表进出口inout物流编号S111S116IBMass Flow kg/hrISOC4H81000.9790 5.4643E-064002.0300 H2O2985.7800 3939.5119.8622 MAL0.0000 0.0000 0.0000 O20.0000 0.0000 0.0000 N20.0000 0.0000 0.0000 CH4O0.0000 0.0000 0.0000 MMA0.0000 0.0000 0.0000 N-HEX-010.0000 0.0000 0.0000 C3H61.6815E-083.7623E-170.0000 C3H88.7563E-081.3189E-150.0000 NC4H103.8305 0.0002566893.8303 ISOC4H100.0801 4.7890E-070.0801 1C4H80.2710 1.0806E-060.2710 CISC4H81.1551 4.5097E-051.1551 TRANC4H80.4776 9.0623E-060.4775 13C4H60.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 TBA4042.8490 78.2006 0.0050 CO0.0000 0.0000 0.0000 CO20.0000 0.0000 0.0000 MAA0.0000 0.0000 0.0000 HQ0.0000 0.0000 0.0000 Total Flow kmol/hr238.2202 219.7311 71.9766 Total Flow kg/hr8035.4230 4017.7120 4017.7120 Total Flow l/min170.8351 76.5599 7970.2860 Temperature 70.1173 134.9165 30.0895 Pressure atm3.4542 3.4878 3.4542 Vapor Frac0.0000 0.0000 1.0000 Liquid Frac1.0000 1.0000 0.0000 Enthalpy Gcal/hr-15.7941 -14.5552 -0.3265 4.2 甲基丙烯醛合成工段图4-3 甲基丙烯醛合成工段工艺流程简图图4-4 甲基丙烯醛合成工段工艺流程简图图4-5 甲基丙烯醛合成工段工艺流程见图本工段主要有氧化酯化反应器、急冷吸收塔、气液分离罐以及双效精馏塔组成，主要工艺设备热量衡算如下。4.2.1 R0201甲基丙烯醛合成反应器表4-6 甲基丙烯醛合成反应器R0201进出口物流表进出口inout物流编号S203S204Mass Flow kg/hrISOC4H84002.0300 144.9465 H2O1295.7930 2563.1310 MAL0.0000 4687.2540 O22351.9120 62.3790 N27745.7270 7745.7270 CH4O0.0000 0.0000 MMA0.0000 0.0000 N-HEX-010.0000 0.0000 C3H61.6815E-081.6815E-08C3H88.7563E-088.7563E-08NC4H103.8303 3.8303 ISOC4H100.0801 0.0801 1C4H80.2710 0.2710 CISC4H81.1551 1.1551 TRANC4H80.4775 0.4775 13C4H60.0000 0.0000 NC5H120.0000 0.0000 ISOC5H120.0000 0.0000 TBA0.0050 0.0050 CO0.0000 29.9426 CO20.0000 47.0456 MAA0.0000 115.0363 HQ0.0000 0.0000 Total Flow kmol/hr493.3566 493.7575 Total Flow kg/hr15401.2800 15401.2800 Total Flow l/min283974.0000 284041.0000 Temperature C350.0000 350.0000 Pressure atm1.4804 1.4804 Vapor Frac1.0000 1.0000 Liquid Frac0.0000 0.0000 Enthalpy cal/sec-2.7732 -8.5998 4.2.2 T0201急冷吸收塔表4-7 急冷吸收塔T0201进出口物流表进出口inoutMass Flow kg/hr物流编号MEOHS205S206S207S209ISOC4H80.0000 144.9465 5.6335 3.2082 147.3717 H2O0.0000 2563.1310 9.5999 2570.7130 2.0187 MAL0.0000 4687.2540 3.4162 4688.8180 1.8518 O20.0000 62.3790 0.0252 0.0148 62.3894 N20.0000 7745.7270 2.0158 1.2299 7746.5130 CH4O3301.4300 0.0000 16613.3200 10285.8500 9628.9000 MMA0.0000 0.0000 0.0005 0.0002 0.0004 N-HEX-010.0000 0.00004.9573E-082.5694E-164.9573E-08C3H60.0000 1.6815E-081.4072E-093.1046E-101.7911E-08C3H80.0000 8.7563E-081.8027E-086.2366E-099.9353E-08NC4H100.0000 3.8303 1.0288 0.1733 4.6858 ISOC4H100.0000 0.0801 0.0411 0.0142 0.1071 1C4H80.0000 0.2710 0.1471 0.0488 0.3694 CISC4H80.0000 1.1551 0.8803 0.2766 1.7588 TRANC4H80.0000 0.4775 0.3327 0.1063 0.7040 13C4H60.0000 0.0000 0.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 0.0000 0.0000 TBA0.0000 0.0050 0.0000 0.0050 7.5425E-11CO0.0000 29.9426 0.1763 0.0494 30.0695 CO20.0000 47.0456 2.9980 1.0273 49.0163 MAA0.0000 115.0363 0.0000 115.0363 5.8727E-16HQ0.0000 0.0000 1.0000 1.0000 1.1116E-05Total Flow kmol/hr103.0339 493.7575 519.3641 532.0852 584.0703 Total Flow kg/hr3301.4300 15401.2800 16640.6200 17667.5700 17675.7600 Total Flow l/min69.9206 238282.0000 352.4320 375.0805 218048.0000 Temperature 30.0000 250.0000 29.9994 59.3117 52.3270 Pressure atm1.1843 1.4804 1.1843 1.2021 1.1843 Vapor Frac0.0000 1.0000 0.0000 0.0000 1.0000 Liquid Frac1.0000 0.0000 1.0000 1.0000 0.0000 Enthalpy Gcal/hr-5.8561 -9.1687 -29.5166 -30.1014 -14.4400 4.2.3 V0201气液分离罐表4-8 气液分离罐V0201进出口物流表 进出口inout物流编号S210S211S212Mass Flow kg/hrISOC4H8147.3717 142.0932 5.2786 H2O2.0187 0.1491 1.8697 MAL1.8518 0.3397 1.5121 O262.3894 62.3688 0.0206 N27746.5130 7744.8170 1.6966 CH4O9628.9000 2033.4240 7595.4760 MMA0.0004 0.0001 0.0003 N-HEX-014.9573E-083.9348E-081.0225E-08C3H61.7911E-081.7724E-081.8707E-10C3H89.9353E-089.0030E-089.3233E-09NC4H104.6858 4.5629 0.1228 ISOC4H100.1071 0.0825 0.0245 1C4H80.3694 0.2818 0.0875 CISC4H81.7588 1.2349 0.5239 TRANC4H80.7040 0.5060 0.1980 13C4H60.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 TBA7.5425E-113.9293E-127.1496E-11CO30.0694930.004040.0654545CO249.0163 48.0147 1.0016 MAA0.0000 0.0000 0.0000 HQ1.1116E-050.0000 1.1116E-05Total Flow kmol/hr584.0703 346.7013 237.3690 Total Flow kg/hr17675.7600 10067.8800 7607.8780 Total Flow l/min121228.0000 121067.0000 161.1629 Temperature 30.0000 30.0000 30.0000 Pressure atm1.1843 1.1843 1.1843 Vapor Frac0.5936 1.0000 0.0000 Liquid Frac0.4064 0.0000 1.0000 Enthalpy Gcal/hr-16.6624 -3.1783 -13.4841 4.2.4 T0202共沸精馏塔表4-9 共沸精馏塔T0202进出口物流表进出口inout物流编号S207S208MAL-MEOHMass Flow kg/hrISOC4H83.2082 0.0000 3.2082 H2O2570.7130 2567.1580 3.5546 MAL4688.8180 1.4150 4687.4030 O20.0148 0.0000 0.0148 N21.2299 0.0000 1.2299 CH4O10285.8500 0.3913 10285.4600 MMA0.0002 0.0000 0.0002 N-HEX-010.0000 0.0000 0.0000 C3H63.1046E-100.0000 3.1046E-10C3H86.2366E-090.0000 6.2366E-09NC4H100.1733 0.0000 0.1733 ISOC4H100.0142 0.0000 0.0142 1C4H80.0488 0.0000 0.0488 CISC4H80.2766 0.0000 0.2766 TRANC4H80.1063 0.0000 0.1063 13C4H60.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 TBA0.0050 0.0000 0.0050 CO0.0494 0.0000 0.0494 CO21.0273 0.0000 1.0273 MAA115.0363 115.0362 6.4126E-26HQ1.0000 1.0000 9.4847E-77Total Flow kmol/hr532.0852 143.8766 388.2086 Total Flow kg/hr17667.5700 2685.0000 14982.5700 Total Flow l/min375.0805 48.9171 322.6312 Temperature 59.3117 100.7401 52.6910 Pressure atm1.2021 1.0363 0.9869 Vapor Frac0.0000 0.0000 0.0000 Liquid Frac1.0000 1.0000 1.0000 Enthalpy Gcal/hr-30.1014 -9.6516 3.2082 4.2.5 T0203甲醇回收塔表4-10 甲醇回收塔T0203进出口物流表进出口inout物流编号H2O-R2H2O-R3S211S213S214Mass Flow kg/hrISOC4H80.0000 0.0000 147.3717 0.3549 141.7383 H2O2567.1580 14031.9000 2.0187 16255.7500 343.4525 MAL1.4150 0.0055 1.8518 1.3862 0.3739 O20.0000 0.0000 62.3894 0.0046 62.3642 N20.0000 0.0000 7746.5130 0.3192 7744.4970 CH4O0.3913 1.6017 9628.9000 2035.0380 0.3789 MMA0.0000 0.0000 0.0004 8.8568E-068.0433E-05N-HEX-010.0000 0.0000 4.9573E-080.0000 0.0000 C3H60.0000 0.0000 1.7911E-080.0000 0.0000 C3H80.0000 0.0000 9.9353E-080.0000 0.0000 NC4H100.0000 0.0000 4.6858 0.9058 3.6571 ISOC4H100.0000 0.0000 0.1071 0.0152 0.0673 1C4H80.0000 0.0000 0.3694 0.0551 0.2267 CISC4H80.0000 0.0000 1.7588 0.3106 0.9243 TRANC4H80.0000 0.0000 0.7040 0.1194 0.3866 13C4H60.0000 0.0000 0.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 0.0000 0.0000 TBA0.0000 0.0000 7.5425E-110.0000 0.0000 CO0.0000 0.0000 30.069490.1108 29.8932 CO20.0000 0.0000 49.0163 1.9963 46.0184 MAA115.0362 560.1644 0.0000 648.6347 26.5659 HQ1.0000 6.3312 1.1116E-057.3311 0.0001 Total Flow kmol/hr143.8766 785.5029 584.0703 973.5549 302.5258 Total Flow kg/hr2685.0000 14600.0000 17675.7600 18952.3300 8400.5450 Total Flow l/min45.3260 246.3883 121228.0000 336.7547 129946.0000 Temperature 30.0000 30.0000 30.0000 51.1684 37.0591 Pressure atm1.0363 0.9869 1.1843 1.0244 0.9869 Vapor Frac0.0000 0.0000 0.5936 0.0000 1.0000 Liquid Frac1.0000 1.0000 0.4064 1.0000 0.0000 Enthalpy Gcal/hr-9.8460 -53.7356 -16.6624 -65.5177 -1.2422 4.2.6 T0204甲醇-水精馏塔表4-11 甲醇-水精馏塔T0204进出口物流表进出口inout物流编号S222S216S217S218Mass Flow kg/hrISOC4H815.2312 5.6335 20.8647 0.0000 H2O13.9363 16257.6200 19.0908 16252.4700 MAL0.0015 2.8984 0.0021 2.8978 O20.0681 0.0252 0.0933 0.0000 N25.4502 2.0158 7.4660 0.0000 CH4O12496.5500 9630.5140 17118.5600 5008.5030 MMA0.0007 0.0003 0.0010 0.0000 N-HEX-012.7568E-081.0233E-083.7765E-080.0000 C3H63.8047E-091.4072E-095.2119E-090.0000 C3H84.8740E-081.8030E-086.6767E-080.0000 NC4H102.7811 1.0287 3.8098 1.1674E-05ISOC4H100.1070 0.0398 0.1465 0.0002 1C4H80.3849 0.1427 0.5273 0.0003 CISC4H82.2481 0.8345 3.0796 0.0030 TRANC4H80.8557 0.3174 1.1722 0.0009 13C4H60.0000 0.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 0.0000 TBA0.0000 7.43E-110.0000 0.0000 CO0.4766 0.1763 0.6529 0.0000 CO28.1055 2.9979 11.1035 0.0000 MAA0.0000 648.6347 0.0000 648.6347 HQ0.0000 7.3311 0.0000 7.3311 Total Flow kmol/hr391.5581 1210.9240 536.3810 1066.1010 Total Flow kg/hr12546.2000 26560.2100 17186.5700 21919.8400 Total Flow l/min312.7034 505.3495 34654.7100 464.1072 Temperature 118.4242 51.4493 128.2730 155.5244 Pressure atm7.8954 14.8039 7.8954 7.9428 Vapor Frac0.0000 0.0000 1.0000 0.0000 Liquid Frac1.0000 1.0000 0.0000 1.0000 Enthalpy Gcal/hr-21.3227 -78.9849 -25.1814 -68.2417 4.2.7 T0205甲醇-水精馏塔表4-12 甲醇-水精馏塔T0205进出口物流表进出口inout物流编号S226S219S220S224Mass Flow kg/hrISOC4H80.0000 0.0000 0.0000 0.0000 H2O24372.0300 16252.4700 4.4454 40620.0600 MAL0.0095 2.8978 2.8917 0.0159 O20.0000 0.0000 0.0000 0.0000 N20.0000 0.0000 0.0000 0.0000 CH4O2.7821 5008.5030 5006.6490 4.6368 MMA0.0000 0.0000 0.0000 0.0000 N-HEX-010.0000 0.0000 0.0000 0.0000 C3H60.0000 0.0000 0.0000 0.0000 C3H80.0000 0.0000 0.0000 0.0000 NC4H100.0000 1.1674E-051.1674E-050.0000 ISOC4H100.0000 0.0002 0.0002 0.0000 1C4H80.0000 0.0003 0.0003 0.0000 CISC4H80.0000 0.0030 0.0030 0.0000 TRANC4H80.0000 0.0009 0.0009 0.0000 13C4H60.0000 0.0000 0.0000 0.0000 NC5H120.0000 0.0000 0.0000 0.0000 ISOC5H120.0000 0.0000 0.0000 0.0000 TBA0.0000 0.0000 0.0000 0.0000 CO0.0000 0.0000 0.0000 0.0000 CO20.0000 0.0000 0.0000 0.0000 MAA972.9508 648.6347 0.0000 1621.5850 HQ10.9967 7.3311 0.0000 18.3279 Total Flow kmol/hr1364.3420 1066.1010 156.5400 2273.903