异丙基苯的生产.pdf

1.先输入物料的成分

选择物性方法为“RK-SOAVE”方法

绘制流程图

设置FEED物流参数

设置cooler参数

设置flash参数

设置reactor参数

运行后，得到结果
COOL-OUTFEEDPRODUCTREAC-OUTRECYCLE

TemperatureF130220130.1190.5130.1
Pressurepsia14.5963614.69614.69614.696
VaporFrac0.056100.0941
MoleFlowlbmol/hr44.3688041.91144.3682.457
MassFlowlb/hr4919.6794807.7714807.7824919.669111.898
VolumeFlowcuft/hr1148.52215648.189.9542035.1391045.119
EnthalpyGcal/hr0.470.5010.4630.5090.007
MoleFlowlbmol/hr
C6H61.96401.9111.960.049
PROPY-014.232401.9114.2322.321
C9H1238.176038.08938.1760.086

（2）改变参数，将cooler模块的温度降到100F

得到结果
COOL-OUTFEEDPRODUCTREAC-OUTRECYCLE

TemperatureF100220100.1194.1100.1
Pressurepsia14.5963614.69614.69614.696
VaporFrac0.033100.0981
MoleFlow
lbmol/hr44.1828042.74244.1821.441
MassFlowlb/hr4870.8174807.7714807.764870.82863.057
VolumeFlowcuft/hr681.66715648.188.8942120.404581.168
Enthalpy
Gcal/hr0.4470.5010.4430.5050.004
MoleFlow
lbmol/hr
C6H62.763402.7422.7630.022
PROPY-014.14402.7424.141.398
C9H1237.279037.25837.2790.021
（3）提高转化率至95%

得到结果
COOL-OUTFEEDPRODUCTREAC-OUTRECYCLE

TemperatureF130220130194.4130
Pressurepsia14.5963614.69614.69614.696
VaporFrac0.003100.0341
MoleFlow
lbmol/hr42.018041.91142.010.099
MassFlowlb/hr4812.2874807.7714807.7714812.2874.516
VolumeFlowcuft/hr138.44315648.189.954769.20542.176
Enthalpy
Gcal/hr0.4630.5010.4630.5010
MoleFlow
lbmol/hr
C6H61.913401.9111.9130.002
PROPY-012.005401.9112.0050.094
C9H1238.092038.08938.0920.003