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SAMPLE PROBLEM #9: SAMPLE PROBLEM #9: One thousand Kilogram per hour of a One thousand Kilogram per hour of a 45 % acetone – in – water solution 45 % acetone – in – water solution is to be extracted at 25 is to be extracted at 25 o C in a C in a continuous counter current system continuous counter current system with pure 1,1,2- trichloroethane to with pure 1,1,2- trichloroethane to obtain a raffinate containing 10 wt obtain a raffinate containing 10 wt % actone. Using the following % actone. Using the following equilibrium data determine with an equilibrium data determine with an equilateral triangle diagram: equilateral triangle diagram: a) minimum flow rate of solvent a) minimum flow rate of solvent b) the number of stages required b) the number of stages required for a solvent rate equal to 1.5 for a solvent rate equal to 1.5 times the minimum. times the minimum.

Sample Problem #9

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Page 1: Sample Problem #9

SAMPLE PROBLEM #9:SAMPLE PROBLEM #9:

One thousand Kilogram per hour of a 45 One thousand Kilogram per hour of a 45 % acetone – in – water solution is to be % acetone – in – water solution is to be extracted at 25 extracted at 25 ooC in a continuous counter C in a continuous counter current system with pure 1,1,2- current system with pure 1,1,2- trichloroethane to obtain a raffinate trichloroethane to obtain a raffinate containing 10 wt % actone. Using the containing 10 wt % actone. Using the following equilibrium data determine with following equilibrium data determine with an equilateral triangle diagram:an equilateral triangle diagram:

a) minimum flow rate of solventa) minimum flow rate of solventb) the number of stages required for a b) the number of stages required for a solvent rate equal to 1.5 times the solvent rate equal to 1.5 times the minimum.minimum.

Page 2: Sample Problem #9

AcetoneAcetonewt fractionwt fraction

WaterWaterwt fractionwt fraction

TrichloroeTrichloroethanethane(wt (wt fraction)fraction)

RaffinateRaffinate 0.550.55 0.350.35 0.100.10

0.500.50 0.430.43 0.070.07

0.400.40 0.570.57 0.030.03

0.300.30 0.680.68 0.020.02

0.200.20 0.790.79 0.010.01

0.100.10 0.8950.895 0.0050.005

Page 3: Sample Problem #9

AcetoneAcetonewt fractionwt fraction

WaterWaterwt fractionwt fraction

TrichloroeTrichloroethanethane(wt (wt fraction)fraction)

ExtractExtract 0.60.6 0.130.13 0.270.27

0.50.5 0.040.04 0.460.46

0.40.4 0.030.03 0.570.57

0.30.3 0.020.02 0.680.68

0.20.2 0.0150.015 0.7850.785

0.10.1 0.010.01 0.890.89

Page 4: Sample Problem #9

RaffinateRaffinate

Wt Fraction Wt Fraction AcetoneAcetone

Extract Extract

Wt Fraction Wt Fraction AcetoneAcetone

0.440.44 0.560.56

0.290.29 0.400.40

0.120.12 0.180.18

The Tie Line DataThe Tie Line Data

Page 5: Sample Problem #9

REQUIREDREQUIREDSSn+1 minn+1 min

XXmm

Page 6: Sample Problem #9

SOLUTIONSOLUTION (a) S(a) Sn+1n+1,min detn ,min detn SS11 is detd by trial, so that tie line is detd by trial, so that tie line

from Sfrom S11 passes thru passes thru by inverse-lever arm:by inverse-lever arm:

SSn+1,min n+1,min = 239.67= 239.67

M

M0

0

min,1n

x

xx

L

S

363.0

363.045.0

1000

S min,1n

Page 7: Sample Problem #9

A

L0

Sn+1

M

S1

T W

DXM=0.363

Page 8: Sample Problem #9

(b) Detn of n(b) Detn of n Sn+1 = 1.5 (Sn+1, min) = Sn+1 = 1.5 (Sn+1, min) =

1.5(239.67) = 359.51.5(239.67) = 359.5 to calc act xto calc act xMM

xxMM = 0.331 = 0.331

M

M0

0

1n

x

xx

L

S

M

M

x

x45.0

1000

5.359

Page 9: Sample Problem #9