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Problems                                                            253



                  Table 5.2 Measured data of
                  system performance

                  θ 1       θ 2       F(θ)
                  2.653     2.639     0.948
                  2.625     2.703     0.744
                  1.865     2.699     0.381
                  2.591     3.104     0.393
                  1.337     2.772     0.648
                  1.779     2.699     0.411
                  2.470     2.515     1.162
                  1.265     3.247     0.784




                  Then, compute the constrained minimum along the unit circle with the additional require-
                  ments that both x 1 and x 2 be nonnegative.

                  5.B.1. We wish to use the enzyme whose kinetics, described by (5.51), were studied earlier
                  in this chapter, in an immobilized-enzyme packed bed reactor. Neglecting any internal
                  mass transfer resistance (we assume the enzyme is immobilized in very small pellets), we
                  compute the outlet substrate concentration by solving the ODE-IVP


                            dc S    1         V m c S
                               =−                          c S (W = 0) = c S0       (5.176)
                           dW      α c υ  K m + c S + K  −1 2
                                                     c
                                                   si  S
                                                                          −4
                  c S0 is the substrate concentration in moles, and is constrained to lie in [10 , 2]. W is the mass
                  of enzyme in the reactor in milligrams, and we integrate (5.176) to the total mass W R = 1g.
                                                                                 6
                  The volumetric flow rate v through the reactor is in liters per minute. α c = 10 µmol/mol
                  is a conversion factor, and the kinetic constants are V m = 200 µmol/(min mg E ), K m =
                  0.201 M, K si = 0.5616 M. Plot the inlet substrate concentration c S0 that maximizes the
                  outlet molar flow rate of product, as a function of υ.
                  5.B.2. We wish to optimize the performance of a process with two adjustable parameters.
                  Table 5.2 contains measured data of the cost function that we wish to minimize. Fit to this
                  data some general ( e.g. polynomial) model and use this model to propose a design that you
                  think might have an even lower cost function value. To avoid extrapolating outside of the
                  region of data, use a set of constraints that will limit the amount to which we can search far
                  away from the existing data points.
                  5.B.3. We wish to determine the best path for a road connecting two points in hilly ter-
                              2
                  rain. Let r ∈  be the coordinates of a point in kilometers and let the elevation at that
                  point, also in kilometers, be z(r). We represent the measured ground elevation data as
                  a sum of contributions from individual hills, each hill being represented by a Gaussian
                  function,

                                  N h
                                                              −1
                                  	   [k]      1     [k]             [k]
                            z(r) =   z   exp −  r − r c  ·   [k]  r − r c           (5.177)
                                      max      2
                                  k=1
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