Page 113 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
P. 113

From Figures E3.1(a) and (b), the mole fraction of reactant B is seen to drop to less than the specification
                    of  0.01  (1  mol%)  at  a  time  of  approximately  2.3  h.  This  time,  coupled  with  the  heating  time  of  70.2
                    minutes, gives a total of 3.5 h. However, note that only about 75% of the product remains in the still to be
                    recovered in the next step.


                    Step 5: Cooling and Crystallization of Product


                    The  analysis  of  the  crystallization,  filtration,  drying,  and  packaging  steps  is  beyond  the  scope  of  this
                    analysis. Therefore, it is assumed that the times for each of these steps have been determined through
                    laboratory-scale experiments, and those times are simply stated here. The amount of product crystallized
                    is 80% of the product recovered from the still, or 60% of the 1057.5 kg produced in the reactor (634.5
                    kg.) The time required to cool and crystallize is 2 h.


                    Step 6: Filtration and Drying


                    The time required for filtration and drying is 4 h.


                    Step 7: Packaging


                    The time required for packaging is 1 h.


                    There  are  several  unique  features  of  batch  operations  observed  in Example  3.1.  First,  the  heating,
                    reaction, and separations steps are unsteady state, which is different from the typical steady-state analysis
                    with  which  most  undergraduate  chemical  engineers  are  familiar.  Secondly,  it  is  observed  that  no
                    provision was made to recycle the unreacted raw materials. In Chapter 2, recycle was shown to be a key
                    element of a steady-state chemical process. Raw materials are almost always the largest item in the cost
                    of manufacturing; therefore, recycling unreacted raw materials is essential to ensure profitability. So, how
                    is this done in a batch process? In Example 3.1, the overhead product from the batch distillation contains
                    unreacted raw material and product in the solvent. This could be sent to a holding tank and periodically
                    mixed with a stream containing pure solvent and just enough reactants A and/or B to make up a single
                    charge  to  the  process  in  Step  1.  However,  the  recycling  of  product  to  the  reactor  would  have  to  be
                    investigated  carefully  to  determine  whether  unwanted  side  reactions  take  place  at  higher  product
                    concentrations. Even though an additional tank would need to be purchased, it is almost certain that the
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