Page 387 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
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in Figure 12.3. Clearly, no McCabe-Thiele construction can be made to produce two pure products from
                    the indicated feed. The heavy component can be purified, but an infinite number of stages above the feed
                    would  be  required  just  to  approach  the  azeotropic  concentration,  (x ,  y ),  the  point  where  the
                                                                                                         az   az
                    equilibrium curve crosses the 45° line. There are minimum- and maximum-boiling azeotropes, although
                    minimum-boiling azeotropes (where the azeotrope is at a lower temperature than either pure-component

                    boiling  point)  are  more  common.  Minimum-boiling  azeotropes  arise  from  repulsive  forces  between
                    molecules.  One  way  of  thinking  about  azeotropes  is  that  the  volatility  switches.  In Figure  12.3,
                    Component A is more volatile when it is present below the azeotropic composition, but Component B is
                    more  volatile  when  Component  A  is  present  above  the  azeotropic  composition.  Given  that  simple
                    distillation  exploits  the  difference  in  volatility  between  components,  it  is  easy  to  understand  how  the
                    switch in volatility makes simple distillation impossible.


                    Figure  12.3  X-Y  Diagram  for  Component  A  Forming  a  Minimum-Boiling,  Binary  Azeotrope  with
                    Component B (Constant Pressure)


































                    In the next section, methods for accomplishing distillation-based separations in the presence of azeotropes
                    for binary systems are discussed. In the subsequent section, methods for azeotropic distillation involving
                    three components are discussed.


                    Binary Systems.   The methods used to distill beyond azeotropes in binary systems are illustrated using
                    McCabe-Thiele  diagrams.  Four  of  the  more  popular  methods  are  discussed  here.  A  more  complete
                    discussion is available in any standard separations textbook [15].


                    The more popular methods for breaking binary azeotropes include the following.
                          1.   One distillation column allows separation close to the azeotrope, and then a different separation
                                method is used to complete the purification (Figure 12.4[a]).


                    Figure 12.4 Distillation Arrangements to Separate Binary Azeotropes
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