丙酮-水物系填料精馏塔的课程设计

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tx100092.70.0186.50.0275.80.0566.50.163.40.1562.10.2610.360.40.4600.559.70.6590.758.20.857.50.9570.9556.131R1.5Rmin40%10000tXD97%Xw3%F1388.889XF0.17XD0.91XW0.01F55.87D9.93tF62.84tD57.41tW93.01α5.417089Rmin1.06681L15.89013L'71.76497V'=V25.820131为丙酮2为水tD温度下Cp1

Cp(D)151.0088tW温度下Cp1Cp(W)35.50316t水的密度tF981.621tD984.707tW963.266

00.2530.4250.6240.7550.7980.8150.830.8390.8490.8590.8740.8980.9350.9631q

丙酮水5818

12011010090801

70MFMDMW

WPA

24.8571454.37518.3802845.94123.5638PB

6050022.81

R0.17yq

1.600215

0.528475

162.698Cp2196.694Cp2丙酮的密度

33.71433.956

系列系列0.20.40.60.811.2系列1系列2

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丙酮-水物系填料精馏塔的课程设计