附录3 能量衡算计算书

中粮生化年产11.6万吨醋酸乙烯项目 能量衡算计算书中粮生化年产11.6万吨醋酸乙烯项目能量衡算计算书2019“东华科技-恒逸石化杯”第十三届全国大学生化工设计竞赛合肥工业大学生生步烯团队指导教师：杨则恒、姚运金、张卫新、徐超、范小明、朱文拿团队成员：贾树寅、于竞超、朱旭、方耀、方满娣目录1.1总述21.2 热量衡算原理21.3 热量衡算任务31.4 热量衡算31.4.1乙烯合成工段31.4.2乙烯精制工段81.4.3醋酸乙烯合成工段151.4.4醋酸乙烯精制工段241.5总结371.1总述本项目拟建一套年产11.6万吨醋酸乙烯酯的装置，在全工艺段中伴随着物料从一个体系或单元进入另一个体系或单元，在发生质量传递的同时也伴随着热量的消耗、释放和转化。其中的热量变换数量关系可以由热量衡算求得，对于新设计的车间，可以由此确定设备的热负荷。再根据设备的热负荷大小、所处理物料的性质及工艺要求选择恰当的设备。总而言之，通过下述热量衡算，可以为后续设计工作中提高热量的利用率，降低能耗提供主要依据。 1.2 热量衡算原理工程依据化工设计中关于热量衡算的基本思想和要求，遵循基本规范与实际工艺相结合的原则，进行热量衡算书的编制。其中一个主要依据是热量平衡方程：其中，表示输入设备热量的总和；表示输出设备热量的总和；表示损失热量的总和。对于连续系统：其中，设备的热负荷；输入系统的机械能；离开设备的各物料焓之和；进入设备的各物料焓之和。在进行全厂热量衡算时，是以单元设备为基本单位，考虑由机械能转换、化学反应释放和单纯的物理变化带来的热量变化。最终对全工艺段进行系统级的热量平衡计算，进而用于指导节能降耗设计工作。1.3 热量衡算任务在进行生物质乙醇资源化利用装置的热量衡算中，主要通过定量计算完成下述基本任务：确定工艺单元中物料输送机械（如泵）所需要的功率，以便于进行设备的设计和选型； 确定精馏等单元操作中所需要的热量或冷量以及传递速率，计算换热设备的尺寸，确定加热剂和冷却剂的消耗量，为后续设计中比如供汽、供冷、供水等专业提供设备条件；确定为保持一定反应温度所需移除或者加入的热传递速率，指导反应器的设计和选型；提高热量内部集成度，充分利用余热，提高能量利用率，降低能耗；最终计算出总需求能量和能量的费用，并由此确定工艺过程在经济上的可行性。1.4 热量衡算1.4.1乙烯合成工段1.4.1.1压缩机热量衡算（1）C0201压缩机表1-1 热负荷表WQHeat Duty（Gcal/hr）1.04340表1-2 流股焓变计算表InOut物流编号02040205Temperature（）45.363777.3968Pressure（bar）1.01331.5000Vapor Frac1.00001.0000Mole Flow（kmol/hr）2883.84022883.8402Mass Flow（kg/hr）81754.187981754.1879Volume Flow（cum/hr）75371.979856034.2028Enthalpy（Gcal/hr）8.11639.1597表1-3 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error1.043408.11639.159701.4.1.2换热器热量衡算（1）E0101原料加热器表1-4 热负荷表WQHeat Duty（Gcal/hr）035.68表1-5 流股焓变计算表InOut物流编号FEEDS0101Temperature（）25.000082.000Pressure（bar）1.00001.0000Vapor Frac01.0000Mole Flow（kmol/hr）3217.10003217.1000Mass Flow（kg/hr）135120.0000135120.0000Volume Flow（cum/hr）166.930094995.6500Enthalpy（Gcal/hr）-214.1500-178.4700表1-6 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error035.6800-214.1500-178.47000（2）E0103加热器表1-7 热负荷表WQHeat Duty（Gcal/hr）04.9700表1-8 流股焓变计算表InOut物流编号S0102S0103Temperature（）362.7314425.0000Pressure（bar）1.00001.3172Vapor Frac1.00001.0000Mole Flow（kmol/hr）3217.10003217.1000Mass Flow（kg/hr）135120.0000135120.0000Volume Flow（cum/hr）170085.7800141768.8000Enthalpy（Gcal/hr）-159.9200-154.9500表1-9 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error04.9700-159.9200-154.95000（3）E0104加热器表1-10 热负荷表WQHeat Duty（Gcal/hr）08.7300表1-11 流股焓变计算表InOut物流编号S0104S0105Temperature（）314.4300425.0000Pressure（bar）1.32001.3200Vapor Frac1.00001.0000Mole Flow（kmol/hr）4228.47004228.4700Mass Flow（kg/hr）135120.0000135120.0000Volume Flow（cum/hr）170085.7800141768.8000Enthalpy（Gcal/hr）-154.9500-146.2100表1-12 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error08.7300-154.9500-146.2100-0.01（4）E0105加热器表1-13 热负荷表WQHeat Duty（Gcal/hr）07.9300表1-14 流股焓变计算表InOut物流编号S0106S0107Temperature（）323.9700425.0000Pressure（bar）1.32001.3200Vapor Frac1.00001.0000Mole Flow（kmol/hr）4854.16004854.1600Mass Flow（kg/hr）135120.0000135120.0000Volume Flow（cum/hr）182953.6900213909.3400Enthalpy（Gcal/hr）-146.210-138.2800表1-15 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error07.9300-146.2100-138.28000（5）E0201冷却器表1-16热负荷表WQHeat Duty（Gcal/hr）0-0.1335 表1-17 流股焓变计算表InOut物流编号S0201S0202Temperature（）46.006640.0000Pressure（bar）1.01331.0133Vapor Frac0.00000.0000Mole Flow（kmol/hr）1200.00001200.0000Mass Flow（kg/hr）22800.698622800.7020Volume Flow（cum/hr）23.912723.7610Enthalpy（Gcal/hr）-81.3866-81.5201表1-18 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-0.1335 -81.3866-81.520101.4.1.3泵热量衡算（1）P0201 循环水泵表1-19 热负荷表WQHeat Duty（Gcal/hr）0.00050表1-20 流股焓变计算表InOut物流编号S0202S0203Temperature（）40.000040.0237Pressure（bar）1.01331.5133Vapor Frac0.00000.0000Mole Flow（kmol/hr）1200.00001200.0000Mass Flow（kg/hr）22800.702022800.7020Volume Flow（cum/hr）23.761023.7616Enthalpy（Gcal/hr）-81.5201-81.5195表1-21 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0.00050-81.5201-81.5195-0.00011.4.2乙烯精制工段1.4.2.1压缩机热量衡算（1）C0202一级压缩机表2-1 热负荷表WQHeat Duty（Gcal/hr）2.57000表2-2 流股焓变计算表InOut物流编号S0208S0209Temperature（）15.0000102.0780Pressure（bar）1.01153.0000Vapor Frac1.00001.0000Mole Flow（kmol/hr）2593.13902593.1390Mass Flow（kg/hr）74818.053674818.0536Volume Flow（cum/hr）61419.432326966.6524Enthalpy（Gcal/hr）23.911226.4812表2-3 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error2.5700023.911226.48120（2）C0203二级压缩机表2-4 热负荷表WQHeat Duty（Gcal/hr）2.50320表2-5 流股焓变计算表InOut物流编号S0211S0212Temperature（）10.000097.7829Pressure（bar）3.00009.0000Vapor Frac1.00001.0000Mole Flow（kmol/hr）2535.33942535.3394Mass Flow（kg/hr）73009.058473009.0584Volume Flow（cum/hr）19895.67508687.9290Enthalpy（Gcal/hr）27.081829.5850表2-6 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error2.5032027.081829.58500（3）C0204三级压缩机表2-7 热负荷表WQHeat Duty（Gcal/hr）2.44350表2-8 流股焓变计算表InOut物流编号S0214S0215Temperature（）5.000092.6844Pressure（bar）9.000027.0000Vapor Frac1.00001.0000Mole Flow（kmol/hr）2514.05302514.0530Mass Flow（kg/hr）72118.559872118.5598Volume Flow（cum/hr）6460.08522832.1906Enthalpy（Gcal/hr）28.169830.6133表2-9 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error2.4435028.169830.613301.4.2.2换热器热量衡算（1）E0203 一级压缩冷却器表2-10 热负荷表WQHeat Duty（Gcal/hr）0-3.3375 表2-11 流股焓变计算表InOut物流编号S0209S0210Temperature（）102.078010.0000Pressure（bar）3.00003.0000Vapor Frac1.00000.9749Mole Flow（kmol/hr）2593.13902593.1390Mass Flow（kg/hr）74818.053674818.0536Volume Flow（cum/hr）26966.652419840.3070Enthalpy（Gcal/hr）26.481223.1437表2-12 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-3.3375 26.481223.14370（2）E0204二级压缩冷却器表2-13 热负荷表WQHeat Duty（Gcal/hr）0-2.9065表2-14 流股焓变计算表InOut物流编号S0212S0213Temperature（）97.78295.0000Pressure（bar）9.00009.0000Vapor Frac1.00000.9863Mole Flow（kmol/hr）2535.33942535.3394Mass Flow（kg/hr）73009.058473009.0584Volume Flow（cum/hr）8687.92906427.7093Enthalpy（Gcal/hr）29.585026.6785表2-15 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-2.906529.585026.67850（3）E0205三段压缩冷凝器表2-16 热负荷表WQHeat Duty（Gcal/hr）0-3.1136表2-17 流股焓变计算表InOut物流编号S0215S0216Temperature（）92.6844-5.0000Pressure（bar）27.000027.0000Vapor Frac1.00000.9453Mole Flow（kmol/hr）2514.05302514.0530Mass Flow（kg/hr）72118.559872118.5598Volume Flow（cum/hr）2832.19061972.2156Enthalpy（Gcal/hr）30.613327.4997表2-18热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-3.113630.613327.49970（4）E0206深度冷凝器表2-19 热负荷表WQHeat Duty（Gcal/hr）0-5.8354表2-20 流股焓变计算表InOut物流编号S0218S0219Temperature（）-5.0000-28.0000Pressure（bar）27.000027.0000Vapor Frac0.98250.0000Mole Flow（kmol/hr）2490.79582490.7958Mass Flow（kg/hr）70589.489770589.4897Volume Flow（cum/hr）2023.9990160.0530Enthalpy（Gcal/hr）29.171023.3356表2-21 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-5.835429.171023.335601.4.2.3塔热量衡算（1）T0202 碱洗塔表2-22 热负荷表WQHeat Duty（Gcal/hr）00表2-23 流股焓变计算表InOut物流编号NAOHS0205RICHOUTS0206Temperature（）21.0077.4051.0650.12Pressure（bar）1.031.501.011.01Vapor Frac0.001.000.001.00Mole Flow（kmol/hr）594.762883.84533.892944.50Mass Flow（kg/hr）10790.1081754.199961.0082583.28Volume Flow（cum/hr）10.0056034.209.4077792.98Enthalpy（Gcal/hr）-40.209.16-35.774.73表2-24 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00-31.0404 -31.0404 0（2）T0203脱重塔表2-25 热负荷表WQHeat Duty（Gcal/hr）04.4286表2-26流股焓变计算表InOut物流编号S0220HCS0221Temperature（）-13.51100.18-25.44Pressure（bar）22.0022.0022.00Vapor Frac0.000.001.00Mole Flow（kmol/hr）2490.8019.212471.58Mass Flow（kg/hr）70589.491271.7669317.73Volume Flow（cum/hr）174.972.241629.71Enthalpy（Gcal/hr）23.34-0.9928.75表2-27 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error04.428623.3427.7600-0.0086（3）T0204 脱轻塔表2-28热负荷表WQHeat Duty（Gcal/hr）00.5877表2-29 流股焓变计算表InOut物流编号S0223RES0224Temperature（）-40.00-25.76-25.44Pressure（bar）22.0022.0022.00Vapor Frac0.001.000.00Mole Flow（kmol/hr）2726.87257.182469.69Mass Flow（kg/hr）76458.147176.7169281.44Volume Flow（cum/hr）165.43170.16161.21Enthalpy（Gcal/hr）25.982.9723.59表2-30 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00.587725.9826.5600-0.00771.4.2.4汽液分离衡算（1）V0201气液分离器表2-31 热负荷表WQHeat Duty（Gcal/hr）00.0680表2-32流股焓变计算表InOut物流编号S0207S0208WATER3Temperature（）15.000015.000015.0000Pressure（bar）1.01151.01151.0115Vapor Frac0.87401.00000.0000Mole Flow（kmol/hr）2944.50092593.1390351.3619Mass Flow（kg/hr）82583.285074818.05367765.2314Volume Flow（cum/hr）60531.172661419.43238.2782Enthalpy（Gcal/hr）-0.125923.9112-23.9692表2-33热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00.0680-0.1259-0.0580-0.0001（2）V0202气液分离器表2-34 热负荷表WQHeat Duty（Gcal/hr）00.0222表2-35流股焓变计算表InOut物流编号S0210S0211WATER4Temperature（）10.000010.000010.0000Pressure（bar）3.00003.00003.0000Vapor Frac0.97491.00000.0000Mole Flow（kmol/hr）2593.13902535.339457.7996Mass Flow（kg/hr）74818.053673009.05841808.9952Volume Flow（cum/hr）19840.307019895.67502.0841Enthalpy（Gcal/hr）23.143727.0818-3.9159表2-36热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00.022223.143723.16600.0001（3）V0203气液分离器表2-37 热负荷表WQHeat Duty（Gcal/hr）00.0495表2-38流股焓变计算表InOut物流编号S0213S0214WATER5Temperature（）5.00005.00005.0000Pressure（bar）9.00009.00009.0000Vapor Frac0.98631.00000.0000Mole Flow（kmol/hr）2535.33942514.053021.2864Mass Flow（kg/hr）73009.058472118.5598890.4986Volume Flow（cum/hr）6427.70936427.70931.0762Enthalpy（Gcal/hr）26.678528.1698-1.4418表2-39热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00.049526.678526.72800（4）V0204气液分离器表2-40 热负荷表WQHeat Duty（Gcal/hr）00.2268表2-41流股焓变计算表InOut物流编号S0216S0217WATER6Temperature（）-5.0000-5.0000-5.0000Pressure（bar）27.000027.000027.0000Vapor Frac0.94531.00000.0000Mole Flow（kmol/hr）2514.05302491.055022.9980Mass Flow（kg/hr）72118.559870594.15891524.4010Volume Flow（cum/hr）1972.21562056.95422.0016Enthalpy（Gcal/hr）27.499729.2833-1.5568表2-42热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00.226827.499727.726501.4.3醋酸乙烯合成工段1.4.3.1压缩机热量衡算（1）C0301压缩机表3-1热负荷表WQHeat Duty（Gcal/hr）0.91880表3-2流股焓变计算表InOut物流编号S03080309Temperature（）49.850091.9608Pressure（bar）5.978210.0000Vapor Frac1.00001.0000Mole Flow（kmol/hr）1883.29491883.2949Mass Flow（kg/hr）55026.292155026.2921Volume Flow（cum/hr）8460.17765717.0271Enthalpy（Gcal/hr）17.740618.6593表3-3 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0.9188017.740618.6593-0.0001（2）C0302压缩机表3-4 热负荷表WQHeat Duty（Gcal/hr）-0.07020表3-5 流股焓变计算表InOut物流编号S0312S0313Temperature（）18.79246.5268Pressure（bar）2.00001.0000Vapor Frac1.00001.0000Mole Flow（kmol/hr）250.0000250.0000Mass Flow（kg/hr）14530.850014530.8500Volume Flow（cum/hr）3034.13195813.3138Enthalpy（Gcal/hr）-7.5474-7.6176表3-6 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error-0.07020-7.5474-7.617601.4.3.2换热器热量衡算（1）E0301反应进料加热器表3-7 热负荷表WQHeat Duty（Gcal/hr）00.0994表3-8 流股焓变计算表InOut物流编号O2INS0304Temperature（）25.0000149.8500Pressure（bar）1.00001.0000Vapor Frac1.00001.0000Mole Flow（kmol/hr）112.0000112.0000Mass Flow（kg/hr）3583.86563583.8656Volume Flow（cum/hr）2776.38763938.9970Enthalpy（Gcal/hr）0.00000.0994表3-9 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00.09940.00000.09940（2）E0302反应进料加热器表3-10 热负荷表WQHeat Duty（Gcal/hr）010.5267表3-11 流股焓变计算表InOut物流编号S0302S0303Temperature（）32.1427149.8500Pressure（bar）1.00006.6875Vapor Frac0.68921.0000Mole Flow（kmol/hr）3086.93623086.9362Mass Flow（kg/hr）118360.3560118360.3560Volume Flow（cum/hr）54052.936816234.3434Enthalpy（Gcal/hr）-83.2967-72.7700表3-12 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error010.5267-83.2967-72.77000（3）E0304朗肯循环冷却器表3-13 热负荷表WQHeat Duty（Gcal/hr）0-1.3804表3-14 流股焓变计算表InOut物流编号S0313S0314Temperature（）6.5268-0.8784Pressure（bar）1.00001.0000Vapor Frac1.00000.0000Mole Flow（kmol/hr）250.0000250.0000Mass Flow（kg/hr）14530.850014530.8500Volume Flow（cum/hr）5813.313824.0962Enthalpy（Gcal/hr）-7.6176-8.9980表3-15 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-1.3804-7.6176-8.99800（4）E0305 冷却器表3-16 热负荷表WQHeat Duty（Gcal/hr）01.7514表3-17 流股焓变计算表InOut物流编号S0316S0317Temperature（）5.000090.0000Pressure（bar）9.00009.0000Vapor Frac1.00001.0000Mole Flow（kmol/hr）1907.31101907.3110Mass Flow（kg/hr）53929.709153929.7091Volume Flow（cum/hr）4901.00716398.7083Enthalpy（Gcal/hr）21.419523.1709表3-18 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error01.751421.419523.17090（5）E0307 冷却器表3-19 热负荷表WQHeat Duty（Gcal/hr）0-0.3185表3-20 流股焓变计算表InOut物流编号S0331S0332Temperature（）75.959440.0000Pressure（bar）1.21591.2159Vapor Frac0.00130.0000Mole Flow（kmol/hr）420.5046420.5046Mass Flow（kg/hr）10154.303510154.3035Volume Flow（cum/hr）22.58589.2906Enthalpy（Gcal/hr）-28.5697-28.8882表3-21 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-0.3185-28.5697-28.888201.4.3.3泵热量衡算（1）P0301丙烷循环泵表3-22热负荷表WQHeat Duty（Gcal/hr）0.00110表3-23 流股焓变计算表InOut物流编号S0314S0311Temperature（）-0.8784-0.7559Pressure（bar）1.00002.0000Vapor Frac0.00000.0000Mole Flow（kmol/hr）250.0000250.0000Mass Flow（kg/hr）14530.850014530.8500Volume Flow（cum/hr）24.096224.1015Enthalpy（Gcal/hr）-8.9980-8.9969表3-24 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0.00110-8.9980-8.996901.4.3.4反应器热量衡算（1）R0302醋酸乙烯合成反应器表3-25热负荷表WQHeat Duty（Gcal/hr）0-7.2366表3-26 流股焓变计算表InOut物流编号S0306S0307Temperature（）159.8500181.8500Pressure（bar）6.68756.6875Vapor Frac1.00001.0000Mole Flow（kmol/hr）3194.33743107.9339Mass Flow（kg/hr）121944.2216121945.3855Volume Flow（cum/hr）17196.315017581.2554Enthalpy（Gcal/hr）-73.7091-80.9457表3-27 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error0-7.2366-73.7091-80.94570.1.4.3.5塔热量衡算（1）T0301 醋酸洗塔表3-28热负荷表WQHeat Duty（Gcal/hr）00表3-29 流股焓变计算表InOut物流编号S0452S0310S0315S0402Temperature（）5.000033.712663.032341.1405Pressure（bar）3.000010.00008.80008.8000Vapor Frac0.00000.98341.00000.0000Mole Flow（kmol/hr）100.00001883.29491886.162397.1326Mass Flow（kg/hr）5970.696755026.292154994.23056002.7583Volume Flow（cum/hr）5.44554727.00865740.02265.9912Enthalpy（Gcal/hr）-10.923317.209816.2728-9.9835表3-30 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error006.2900 6.2900 0（2）T0302 二氧化碳吸收塔表3-31热负荷表WQHeat Duty（Gcal/hr）00表3-32 流股焓变计算表InOut物流编号S0318MEAS0320S0321Temperature（）90.000040.000040.289443.0993Pressure（bar）9.00001.21591.01331.2132Vapor Frac1.00000.00051.00000.0000Mole Flow（kmol/hr）1901.1971417.50962013.5961289.0974Mass Flow（kg/hr）53591.10089917.678955208.66148300.1183Volume Flow（cum/hr）6378.197013.089951508.72058.5063Enthalpy（Gcal/hr）23.4985-28.566716.5369-21.6051表3-33 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error00-5.0682 -5.0681 -0.0001（3）T0303 二氧化碳解吸塔表3-34热负荷表WQHeat Duty（Gcal/hr）01.2704 表3-35 流股焓变计算表InOut物流编号S0322S0323S0324Temperature（）90.000095.4987116.1089Pressure（bar）1.21321.01331.2159Vapor Frac0.00001.00000.0000Mole Flow（kmol/hr）289.0974100.0000204.0354Mass Flow（kg/hr）8300.11832189.92346110.1945Volume Flow（cum/hr）8.76483005.18465.6252Enthalpy（Gcal/hr）-21.3244-6.2596-13.7944表3-36 热量平衡计算表一览W（Gcal/hr）Q（Gcal/hr）Hin（Gcal/hr）Hout（Gcal/hr）Error01.2704 -21.3244-20.0540 01.4.3.6