Flash Vaporization: If a liquid of known composition is
vaporized in one stage, then the composition of the liquid and vapor after
separation can be found as
|
|
A
component balance gives
|
|
Which
can be rearranged to give
|
|
This
line passes through point 1(xF,xF) and has a slope
of -W/D. Intersection of this
line with the equilibrium curve yields point 2(x,y) that gives
composition of vapor y, and a liquid of a composition x leaving
the separator.
Knowing
the equilibrium composition, we can find the temperature in the separator. Both liquid and vapor are at same
temperature. We can either use bubble-
or dew point equation to find the temperature.
Example
6.5: A liquid mixture contains two
components. Component A is present at a
concentration of 50 mol %. Component B
is also present at a concentration of 50 mol %. The feed is at a temperature of 80 °F.
This feed is continuously flash vaporized at a pressure of 1 atm to vaporize 60 mol % of the feed. What will be the composition of the vapor
and liquid leaving the flash separator?
Relative volatility at conditions within separator is 2.16. Component A is more volatile.
Solution: Basis: 100
lbmol of feed.
For
60 % vaporization, amount of distillate obtained after condensation of vapors
is
|
|
Draw
operating line having a slope -0.667 and passing through point (0.5, 0.5). We can draw equilibrium curve using the
following equation.
|
|
It
can be seen that intersection of operating line and equilibrium line occurs at
(0.386, 0.756). This gives us a
composition of vapor (distillate) as 75.6 % A and 24.4 % B. The composition of liquid is 38.6 % A and
61.4 % B.