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Chapter 8

Chapter 8

8.D2.
  1. Butanol product = 3743.45 and water product = 1256.55 kmol/h

  2. Column 1: Optimum feed is stage 3 below condenser, and need 3 stages + partial reboiler.

    Column 2: Need ~ 2/3 stage + partial reboiler.

8.D8.Must convert wt frac to mole Frac, αwater-ether_in_ether_layer = 7.026 (L/D)min = 7.467, L/D = 11.2, Top stage is opt. feed and need ~4 3/5 equilibrium contacts.
8.D10.
  1. T = 97.5°C

  2. nwater/norganic = 10.81


  

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