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316    Chapter 11 Distillation





             11.5 Design illustration e fractionator
             Design Problem
                                                                 3
                Benzene is proposed to be recovered by fractionating a 20 m /hr stream containing 35%, 25% and
             40% mol benzene, toluene and ortho-xylene (O-x). At least 75% of the benzene in feed needs to be
             recovered with 95% purity. Component property data are provided in Table 11.7.
                Make a quick design of the fractionator.

               Table 11.7 Component property data.
                                         Benzene (B)        Toluene (T)        Ortho-xylene (O-x)
               Molecular weight (MW)     78                 92                 106
               N.B.P. (K)                353.05             383.6              417.4
               Density, r (gm/cc)        0.8787             0.8636             0.8800
                                          sat
               Constants in Antoine’s equation log 10 (p ) ¼ a b/(T þ c);p sat  (saturated vapor pressure) in kPa, T in C.

               a                         6.01905            6.08436            6.12699
               b                         1204.637           1347.620           1476.753
               c                         220.089            219.787            213.911
               Cp l (kJ/kmol K),         134.8              155.96             187
               average
               Cp v (kJ/kmol K),         82.44              103.7              132.5
               average
               Heat of vaporisation at   30.77              38.06              36.24
               NBP, l (kJ/kmol)



                The l value at temperatures T 1 and T 2 are related by the equation
                (l 1 /l 2 ) ¼ {(T c   T 1) /(T c   T 2 )} 0.38 , where T c is the critical temperature of the component.
                Solution
                Feed

                                  MW F ¼ð:35   78 þ :25   92 þ :4   106Þ¼ 92:7
                    r ¼ð35   78 þ 92   25 þ 106   40Þ=
                     F
                                                                                        3
                   ð35   78 = :8787 þ 92   25 = :8636 þ 106   40 = :88Þ¼ 0:8755 kg=L ¼ 875:5kg=m
             Hence, F ¼ 875:5   20=92:7 ¼ 1888:9 kg mol/hr; (B ¼ 661.1, T ¼ 472.2, O-x ¼ 755.6 kg mol/hr)

                                        z F ¼ 0:35=0:25=0:4; mole fraction
                Deciding light and heavy key components: As per product specification, Benzene and Toluene are
             set as light and heavy key components. This means that distillate D to have minimum 90 mol%
             Benzene and the rest is Toluene.
                Distillate Composition: Based on 75% benzene recovery and 95% mole purity of benzene,
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