Page 155 - Elements of Chemical Reaction Engineering 3rd Edition
P. 155

Sec. 4.1   Design Structure for  Isothermal Reactors           127

                              our general mole balance equation (level 1) to a specific reactor to arrive at the
                              design  equation for that reactor  (level 2). If  the  feeld  conditions  are  specified
                              (e.g., NAo or FA0). all that is required to evaluate the (design equation is the rate
               Use the algorithm
                    rather than   of reaction as a fuinction of conversion at the same conditions as those at which
                    memorizing   the  reactor  is to  be  operated  (e.g., temperature and pressure).  When  -rA  =
                     equations
                              f(X) is given, one can go directly from level 3 to level 7 to determine either the
                              time or reactor volume necessary to achieve the specified conversion.
                                   If the rate of reaction  is not given explibitly as a function of  conversion,
                              the rate law must be determined (level 4) by either finding it in books or jour-
                              nals  or  by  deterimining  it  experimentally  in  the  laboratory.  Techniques  for
                              obtaining and analyzing rate data to determine the reaction order and rate con-
                              stant are presented  in Chapter 5. After the rate law has been  established,  one
                              has only to use stoichiometry (level 5) together with the conditions of the sys-
                              tem (e.g., constant volume, temperature) to express concentration as a function
                              of  conversion. By combining the information in levels 4 and 5, one can express
                              the rate of  reaction  as a function of  conversion and arrive at level 6. It is now
                              possible  to determine either the  time  or reactor  volume necessary  to  achieve
                               the desired conversion by  substituting the relationship  relating conversion and
                               rate  of  reaction  into the  appropriate  design  equation. The  design  equation  is
                               then  evaluated  in  the  appropriate  manner  (Le.,  analytically  using  a  table  of
                               integrals, or numerically using an ODE solver). Although this structure empha-
                               sizes the determination of a reaction time or volume For  a specified conversion,
                               it can also readily be wed for other types of reactor calculations, such as deler-
                               mining  the conversion for  a specified volume. Different manipulations  can be
                               performed  in level 7 to answer the types of questions mentioned here.
                                   The structure shown in Figure 4-1 allows one to develop a few basic con-
                               cepts and then to arrange the parameters (equations) associated with each con-
                               cept  in  a  variety  of  ways.  Without  such  a  structure,  one  is  faced  with  the
                               possibiliity  of  choosing  or  perhaps  memorizing  the  correct  equation  from  a
                               multitude  of  equations that can arise for a variety of  different reactions,  reac-
                               tors,  and sets of  conditions. The challenge  is to put everything together  in an
                               orderly and logical fashion so that we can proceed to arrive at the correct equa-
                               tion for a given situation.
                                    Fortunately,  by  using  an  algorithm  to  formulate  CRE problems,  which
                               happens  to be analogous to ordering dinner from a fixed-price menu in  a fine
                               French restaurant, we can eliminate virtually all memorization. In both of these
                               algorithms  we must make choices in  each category. For example, in orderling
                               from  a  French  menu,  we  begin  by  choosing  one  dish  from  the  appetiz,ers
                               listed. Step  1 in the  analog in CRE is to begin by  choosing the mole balance
                               for one of the three types of reactors  shown. In step 2 we choose the rate law
                               (eiztre'e), and in step 3 we  specify whether the reaction  is gas or liquid phase
                               (cheese or dessen). Finally, in step 4 we combine steps  1, 2, and 3  and obtain
                               an  analytical  solution  or  solve  the  equations  using  an  ordinary  differential
                               equation (ODE) solver. (See complete French menu on the CD-ROM)
                                    We now will apply this algorithm to a specific situation. The first step is
                               to derive or apply the mole balance  equation for the system at hand.  Suppose
                               that we have,  as shown in Figure 4-2, mole balances  for three reactors,  three
   150   151   152   153   154   155   156   157   158   159   160