Environmental Engineering Reference
In-Depth Information
Thus, if the inlet and outlet compositions are known, then V
O can be determined. For
an extraction process, this corresponds to the required solvent
/
/
diluent flow ratio. The
ratios O
F could be determined with the appropriate substitution in one of the
component balances. [ Remember : these ratios are determined by mass balances around
the control volume. Nothing has been stated about thermodynamic equilibrium within the
control volume.]
Setting these equations equal to each other and rearranging gives:
z B o
/
F and V
/
x B i
y B i
z B o
x A i =
z A o .
(3.31)
z A o
y A i
The left-hand side of this equation is the slope from F to O , and the right-hand side is the
slope from F to V . The equation itself is in the three-point form of a straight line. Hence,
the points ( z A o ,
y B i ) are all on a straight line.
Using the similar triangles in the figure:
z B o ), ( x A i ,
x B i ), and ( y A i ,
FO
VF =
FB
VA =
z B o
x B i
z B o .
(3.32)
y B i
The right-hand side of this equation was already shown to be equal to V
/
O , therefore:
V
O =
FO
VF =
lever-arm rule
.
(3.33)
When applied to extraction problems, the two feed streams V and O are equivalent to the
incoming feed and solvent streams. The stream F would represent a two-phase mixture,
which would separate into the raffinate and extract phases. The component A is usually the
solute and the component B is usually the diluent, although the lever-arm rule will work
no matter how the axes of the diagram are arranged. When solving extraction problems
graphically, it is really useful to remember equations:
Vy A i +
Ox A i
Vy B i +
Ox B i
z A o =
or
z B o =
+
+
O
that help to plot the mixing point without having to re-solve the mass balances. Either one
of these co-ordinates is sufficient to plot the mixing point, since it is already known to be
colinear with the points of the two inlet streams. Remember that the lever-arm rule will
work in any part of the diagram, whether it is two-phase or not (but extraction cannot
perform a separation in the single-phase region) .[ Remember : The end points of the line
correspond to the compositions of the streams, while the ratios of lengths can then be used
to find their flowrates.]
V
O
V
Summary
1 The lever-arm rule is a grap hical alternative to solving a mass balance .
2 The points on the line OFV correspond to the compositions of the various streams.
3 This method is useful for solving:
(a) for a ratio of stream flowrates ( V
O or any other);
(b) for a stream composition ( x A i , etc.).
/
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