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Chapter 13

Chapter 13

13.D4.yout = 0.0075, N = 33.6
13.D7.E = 639.6 kg/h.
13.D9.N = 5.44, Recovery linoleic acid = 87.7%
13.D11.N ~ 8.5 equilibrium stages
13.D14.
  1. yA = 0.115, yw = 0.04, xA = 0.23, xw = 0.73

  2. S = 85.7 kg/h

13.D15.
  1. Column 1, y1 = 0.00092693, yN+1 = 6.929 E-6

  2. Column 2: R = 50.35, xN = 0.0183

13.D21.
  1. yAE = 0.06, yDE = 0.05, xAR = 0.42, xDR = 0.48

  2. E = 214 kg/h

13.D25.
  1. S = 2444 kg/h

  2. N =2

13.D26.

S = 5600, EN = 6830, R1 = 770 kg/h. Extract: 10.5% acetic acid and 3.5% water Raffinate: 5% acetic acid and 93% water

14.D14.

  1. Exit raffinate 27.5% acetic acid and 67.5% water

  2. Entering extract 13% acetic acid and 0.0% water

  3. R1 = 655 kg/h and Entering extract flow rate = 2155 kg/h

13.D38.xout =0.0000275 and yout = 0.0037. If your answer is xout = 0.000102, which is incorrect, you have not been careful with your units.

13.E1.~ 93.5 % m-xylene recovery with 8 stages with feed on stage 4


  

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