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Stage Compositions

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... and the equilibrium curve until one reaches a desired composition coming off the last stage. ... Lecture 13. 6. McCabe-Thiele Stage Solution. Total Reboiler ... – PowerPoint PPT presentation

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Title: Stage Compositions


1
Stage Compositions Total Condenser
2
McCabe-Thiele Graphical Solution Binary
Distillation
  • One can graphically solve a binary distillation
    problem using the McCabe-Thiele method on a y vs.
    x plot using the equilibrium curve and the
    operating lines (mass balances).
  • If one starts at one end of the column, one can
    take advantage of the fact that the mass balance,
    or operating line, provides a link, or the
    relationship, between molar compositions of the
    vapor and liquid streams passing each other
    between stages.
  • The equilibrium relationship provides the
    relationship between the molar compositions of
    the vapor and liquid streams on the stages.
  • One can use these relationships to sequentially
    solve for all of the vapor and liquid molar
    compositions by stepping off along the stages
    the McCabe-Thiele method is a sequential solution
    of all of the internal stage compositions.

3
McCabe-Thiele Graphical Example Total
Condenser
  • If one has a total condenser, one will know that
    xD xo y1 which serves as the starting point
    for the solution.
  • This starting point lies on the intersection of
    the enriching section operating line and the y
    x auxiliary line.
  • This is equivalent to starting the stepping off
    on the operating line at xD.

4
McCabe-Thiele Graphical Example Total
Condenser
  • The vapor molar composition coming off the first
    stage in the column is known since we have a
    total condenser it is y1 xD however, one
    doesnt know the liquid composition, x1, coming
    off stage 1 and flowing down to stage 2.
  • However, one can obtain x1 from the equilibrium
    relationship since y1 is known.
  • Once one has x1, one can determine y2 from the
    operating line since these compositions represent
    passing streams.

5
McCabe-Thiele Graphical Solution
  • One can continue on down the column by stepping
    off between the operating line and the
    equilibrium curve until one reaches a desired
    composition coming off the last stage.
  • The number of step offs obtained is the number
    of stages that will be needed in the column to
    obtain a given separation.

6
McCabe-Thiele Stage Solution Total Reboiler and
Condenser Stepping Down
7
(No Transcript)
8
Complete McCabe-Thiele Solution
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