1000 kg/h of a hydrocarbon mixture containing 25% xylene by mass is fed to an extraction unit which partially removes the xylene by contacting the hydrocarbon stream with 2000 kg/h of an immiscible solvent initially containing 0.5% xylene by mass. The raffinate stream will contain 2% xylene by mass. Calculate the mass flowrates of the extract and raffinate streams and the composition of the extract.
First, let us draw the diagram
Clearly, we can perform the next mass balances:
F + S = E + R
overall mass balance over X:
F*Xf + S*Xs = E*Xe + R*Xr
substitute values:
F + S = E + R turns:
1000+2000 = E + R
F*Xf + S*Xs = E*Xe + R*Xr turns to
1000*0.25 + 0.005*2000 = E*Xe + 0.02*R
we have
3000 = E + R
260 = E*Xe + 0.02*R
Note that:
we have 2 equations and 3 unkown, so
Degrees of Freedom = 3-2 = 1 , we need an extra variable
i.e. set either E, R, or final Xe
We can't assume Xe = 0, since the extract will always have higher concentration than that of the raffinate
So the best conclusions is:
System is not set, it has 1 Degree of Freedom
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