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80    Chapter  Four


             of liquid, that is, Eq.  (4-1), and assume that the process outlet flow
             rate, Y(t}, will also be a sinusoid with the same frequency but with a
             phase relative to U(t), namely,

                                 Y(t) =  Cei<2nft+8)             (4-4)

                Note  that  the  amplitude  of  the  process  outlet  C  is  as  yet
             unknown as is the phase 8. As mentioned in our leap of faith state-
             ment, assume that the actual process outlet flow  rate is  the real
             part of the expression in Eq.  (4-4).  Using Eq.  (4-4)  also assumes
             that after making the process input U a sinusoid, all of the tran-
             sients associated with that change have died out leaving the outlet
             flow rate to be a complex sinusoid with a modified amplitude and
             phase. If  the choice of Eq. (4-4) is incorrect it will show up quickly
             as we turn the crank.
                With  all  these  nontrivial  preliminaries  out of the  way,  put
             Eqs. (4-2) and (4-4) into Eq. (4-1) and see if  something insightful hap-
             pens. A lot of the details will be left to App. B. After plugging in the
             expression for U andY, Eq. (4-1) becomes

                         -r(j2tr  f)Cei<2nft+B) +  Cei<2~rft+B) = Auei<2~rft)

                This messy looking expression is really a simple (but complex)
             equation that has real and imaginary parts. In App. B these real and
             imaginary parts are collected algebraically and the real parts on the
             left-hand side of the above equation are equated to the real parts on
             the right-hand side. The same thing is done with the imaginary parts.
             This gives two equations that, with the help of some inverse trigono-
             metric identities, can be solved for the unknown amplitude C and the
              phase 8. The result is




                                   A                             (4-5)
                            C=      u
                               ~1  +  {2tr  f-r)  2

                 This supports the earlier contention that  as the frequency increases
              the phase lag increases (or the phase becomes more negative) as does
              the amplitude attenuation. It also tells us that as the tank size and its
              associated time constant increase so does the phase lag and the ampli-
              tude attenuation.  Furthermore, it supports our contention that the
              frequency of the process output is the same as that of the input [if this
              were not the case then the idea of plugging in assumed functions for
              U(t)  and Y(t)  would not have worked]. Finally, it suggests that the
              maximum phase lag for this first-order process is 90°.
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