Page 25 - Chemical process engineering design and economics
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12                                                       Chapter 1

           combined and only one compressor is used.  If the conversion is less than  100%, a
           recycle compressor will transfer the unreacted gases back to the reactor after  sepa-
           rating out the products.  Since the recycled gases are already at a high pressure, but
           at a lower pressure than at the reactor inlet because of frictional pressure losses, a
           compressor  is  needed  to  recompress  the  gases  to the reactor  inlet pressure.  This
           step would be considered primarily material transfer.
                Because raw-material  delivery  cannot be  accurately predicated,  on  account
           of unforeseen  events  such  as bad  weather,  strikes,  accidents,  etc., storage  of  raw
           materials is a necessity.  Similarly, the demand for products can be unpredictable.
           Also,  internal  storage  of  chemical  intermediates  may  be  required  to  maintain
           steady operation of a process containing batch operations or to  store chemical in-
           termediates  temporarily  if  downstream  equipment  fails.  Production  can  continue
           when repairs are completed.
                The  last  three  process  operations;  size  reduction,  agglomeration,  and  size
           separation; pertain to  solids.  Examples of  size reduction  are grinding  and  shred-
           ding.  An  example  of  agglomeration  is  compression  of  powders  to  form  tablets.
           Screening to sort out oversized particles is an example of size separation.
                The  first  step in the synthesis, or development and design of a process, is to
           construct a flow  diagram, starting with raw materials and ending with the finished
           product.  The  flow  diagram is a basic tool of a chemical engineer to organize his
           thinking  and  to  communicate  with  other  chemical  engineers.  A  selected  list  of
           flow-diagram  symbols  for  the  process  operations  discussed  above  are  given  in
           Figure  1.2.  Other  symbols  are  given  by  Ulrich  [19] and by  Hill  [20] and  have
           been collected  and reviewed by Austin  [21].  The various process operations dis-
           cussed above, using the flow-diagram symbols in Figure  1.2, are used to describe a
           process  for producing  glucose  from  cornstarch,  which  is  illustrated  in  Example
            1.1.

           Example 1.1  Glucose Production from Corn Starch_______________

           A process flow  diagram for the production of glucose is shown in Figure 3.  Iden-
           tify  each process unit according to the process operations listed in Table 3.
                Although  glucose  could  be  obtained  from  many  different  natural  sources,
           such as  from  various  fruits,  it  is primarily  obtained  by  hydrolysis  of corn  starch,
           which contains about 61% starch.  Starch is a polymer consisting of glucose units
           combined  to  form  either a  linear polymer  called  amylose,  containing  300  to  500
           glucose units, or a branched polymer called amylopectin, containing about  10,000
           glucose units.  Glucose is a crystalline  white  solid, which exists in three isomeric
           forms:  anhydrous  cc-D-glucose,  oc-D-glucose  monohydrate  and  anhydrous  (3-D-
           glucose.  Most of the  glucose produced is used in baked  goods and in confection-
           ery as a sweetener.  It is sold under the trivial name of dextrose, which has evolved
           to mean anhydrous a-D-glucose and a-D-glucose monohydrate.






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