Crosscurrent Extraction:
Locate feed point F having a composition xF of solute A.
Draw a tie-line RE through the point M having composition of xM. Two phases are in equilibrium. Extract rich phase is represented by E having composition xE, whereas raffinate rich phase is represented by R having composition xR.
The overall balance can be represented by Equation 8.1 given below.
Composition of the solvent-free raffinate can be represented by R' on line AC. The point R' can be located by extending the line BR. The point R' has a composition of xR' and is free of solvent.
Composition of the raffinate-free extract can be represented by E' on line AB. The point E' can be located by extending the line CE. The point E' has a composition of xE' and is free of raffinate.
Mixing operation of feed with solvent results in a mixture M having composition xM that lies on line FB.
F + B1 = E1 + R1 = M1
R1 + B2 = E2 + R2 = M2
R2 + B3 = E3 + R3 = M3
Rn-1 +Bn = En + Rn = Mn
Similar calculations can be repeated for additional stages, till we reach a desired concentration in the raffinate phase R.
Immiscible Solvents: If solvents A, and B are immiscible at all concentrations, solution technique is bit different.
Determine xF' = xF /(1 - xF)
Calculate ratio A/B
Locate point F representing the corresponding feed composition.
Draw a line FD from point F with a slope -A/B such that it intersects equilibrium curve
Read the coordinates of point D (x1', y1')
Solute removed = A(xF - x1')
Use appropriate A/B for the following stages.
Draw a perpendicular line from point D till it meets the base at F1.
Draw a line F1E from point F1 with a slope -A/B such that it intersects equilibrium curve.
Read the coordinates of point E(x2', y2').
Repeat this procedure till raffinate concentration reaches the desired value, xn'.
Countercurrent Extraction:
Locate feed point F having a composition xF of solute A.
Draw a line BF representing mixing operation, thus forming a hypothetical mixture M having composition xM such that xM = xFF/(F+B)
Locate the point Rn representing the concentration in the final raffinate xn.
Draw a line RnM and extend it to E1. The point E1 represents the solvent rich phase with a composition of xE1.
Draw line E1F and extend it to Δ such that another line BRn when extended also passes through Δ (difference stream). This fact is represented by Equation 8.6 given as below.
Δ = E1 - F = B - Rn
Draw a tie line E1R1 from E1. The point R1 represents composition of raffinate from 1st stage.
Draw a line ΔR1 and extend to E2 on extract rich phase. The point E2 represents composition of extract from 2nd stage.
Repeat last two steps till composition of raffinate is equal or less than on represented by point Rn.
Minimum amount of solvent Bmin can be found as follows.
Draw a tie line E1minR1min such that when extended passes through F.
Draw a line E1minRn.
Draw another line BF.
Locate point Mmin at the intersection of lines E1minRn and BF.
Calculate Mmin from the mass balance = xFF/ xMmin or any other graphical technique.