学院江山蓝团队-1-设计集71物料衡算表

概 物料衡算原 物料衡算任 物料衡算 泵 概本项目以总厂在省安庆市小区的安庆总厂的尾气处理中的含算、能量衡算，Aspenplus1-11-1Aspenplus物料衡算原—进入系统的物料流率；物料衡算任原料的消耗量，“三废”的排放量以及最后产品的质量指标等关键经济技术指标，对所选工艺路线、设计流程进行定量评述，为后阶段的设计提供依据。物料衡水洗塔4-1（T1）Stream1243TemperaturePressureVapor1001MoleFlowMassFlowVolumeFlow----0000000000000000压缩机（C1-4-2（C1）Stream33-TemperaturePressureVapor11MoleFlowMassFlowVolumeFlow --00004-3（C2）StreamF1-6-Temperature--PressureVapor11MoleFlowMassFlowVolumeFlow --004.60E-4.60E-换热器Stream5-3-6Temperature-PressureVapor01MoleFlowMassFlowVolumeFlow ---000000000000闪蒸罐Stream6F1-F1-Temperature---PressureVapor01MoleFlowMassFlowVolumeFlow ---0004.60E-脱碳塔（T2-4-6（T2）Stream76-98Temperature----PressureVapor0110MoleFlowMassFlowVolumeFlow ----000000000004.60E-6.03E-4.60E-04-7（T3）Stream98Temperature----PressureVapor1010MoleFlowMassFlowVolumeFlow ----00006.03E-4.60E-3.33E-1.26E-4-8（T4）StreamTemperature----PressureVapor1010MoleFlowMassFlowVolumeFlow----00003.33E-1.26E-9.26E-3.67E-换热器（E2-4-9（E2）Stream7-7Temperature-PressureVapor00MoleFlowMassFlowVolumeFlow --0000000000000000004-10（E3）Stream6-6-Temperature--PressureVapor11MoleFlowMassFlowVolumeFlow --004.60E-4.60E-脱硫塔4-11（T5）Stream1-Temperature-----PressureVapor10001MoleFlowMassFlowVolumeFlowEnthalpy-----000000000009.26E-3.67E-09.26E-3.67E-0换热器（E4-Stream1-Temperature--PressureVapor00MoleFlowMassFlowVolumeFlow --003.67E-3.67E-StreamTemperature--PressureVapor00MoleFlowMassFlowVolumeFlow --003.67E-3.67E-Stream1-Temperature--Pressure33Vapor0MoleFlowMassFlowVolumeFlow --003.67E-3.67E-解析塔Stream1-Temperature---PressureVapor10110MoleFlowMassFlowVolumeFlowEnthalpy----01.43E-02.43E-02.16E-0000000003.67E-9.26E-07.10E-4.59E-01.82E-泵StreamTemperature--Pressure8Vapor00MoleFlowMassFlowVolumeFlow --009.26E-9.26E-压缩机StreamTemperature-PressureVapor11MoleFlowMassFlowVolumeFlow --003.67E-3.67E-换热器（E7-StreamTemperature--Pressure86Vapor00MoleFlowMassFlowVolumeFlow --009.26E-9.26E-StreamTemperature--Pressure