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Sec. 7.3   Polymerization                                      357

                                By usiing diols and diacids we can form polymers with two different structural
                                units which together become the repeating  unit. An example of  an ARIA plus
                                BR,B  reaction  is that used  to make Coca-cola@ bottles,  i.e. terephthalic  acid
                                plus ethylene glycol to form poly (ethylene glycol terephthalate).
                                     When discussing the progress of step polymerization it is not meaningful
                                to use conversion of monomer as a measure because the reaction will still pro-
                                ceed even  though  all the monomer  has been  consumed.  For  example,  if  the
                                monomer  A-R-B  has been consumed. The polymerization  is still continu-
                                ing with
                                           A--R,-B   + A-R,-B           A-RS-B    + AB
                                           A-MR5-B  + A-R,-B     + A-R1o-B        + AB

                                because there are both A and B functional groups that can react. Consequently,
                                we measure the progress by the parameter p  which is the fraction of functional
                                groups, A, B,  that  have  reacted.  We  shall  only  consider  reaction  with  equal
                                molar feed of  functional groups. In this case

                                          M, -  - fraction of functional groups of either A or B that
                                      p=---         have reacted
                                            M,

                                     A4 = concentration of either A or B functional groups (mol/dm3)
                                As an example of  step polymerization, consider the polyester reaction in which
                                sulfuric acid is used as a catalyst in a batch reactor. Assuming the rate of  dis-
                                appearance is first order in A, B, and catalyst concentration (which is constant
                                for an externally added catalyst). The balance on A is

                                                          -- -d'A1  - k[AI[Bl                (7-22)
                                                            dt
                                For equal molar feed we have
                                                           [A] = [B] = M

                                                            d'- -_  -kM2
                                                             dt


                                                           M=                                (7-23)
                                                                1 + M,kt
                                In terms of  the fxactional conversion of functional groups, p,

                                                          --  - M,kt+  1                      (7-24)
                                                          1-P
                                                                            ,
                                The number average degree of polymerization,  x,, is the average number  of
                                structural units per chain
                         Degree                            Elipi -
                                                             x,
                  of Polymerization                            =                              (7-.25)
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