Page 135 - Elements of Chemical Reaction Engineering 3rd Edition
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Sec. 3.5   Reactions with Phase Change                          107
                                I   and combining Equations (E3-9.2), (E3-9.4), and (E3-9.8) gives


                                             dFB  -
                                             - rB = -2rA  = 2kACTo
                                                 -
                                             dV
                                   Equations (E3-9.8) and (E3-9.9) can  now  be  solved numerically, preferably  by  a
                                I  software package such as POLYMATH or MATLAB. (See Chapter 4)


                                 3.5  Reactions with Phase Change

                                 When Equation (3-36) is used to evaluate E , it should be remembered from the
                                 derivation of  this equation that 6 represents the change in the number of  moles
                                 in the gas phase per mole of A reacted. As the last example in this chapt, er , we
                                 consider a  gas-phase reaction  in  which  condensation occurs. An  examiple of
                                 this class of reactions is



                                      Another example of phase change during reaction is chemical vapor dep-
                                 osition (CVD), a process used to manufacture microelectronic materials. Here,
                                 gas-phase reactants are deposited (analogous to condensation) as thin films on
                                 solid surfaces (see Problem P3-25). One such reaction is the production of gal-
                                 lium arsenide, which is used in computer chips.

                                         GaC12(g)+~As2(g)+H2(g) --+ GaAs(s)+2HCl(g)

                                 The  development of  continuous-flow CVD  reactors  where  solid  wafers  and
                                 gases continuously pass through the reactor is currently under way  (see: Sec-
                                 tions  10.8 and  12.11).
                                      We  now  will  develop our  stoichiometric table  for reactions  with  phase
                                 change. When one of  the products condenses during the course of  a reaction,
                                 calculation  of  the change in  volume  or  volumetric flow  rate  must  be  under-
                                 taken in a slightly different manner.  Consider anoiher isothermal reaction:

                                                  A (g) + 2B (g) -  3- D (g, 1)
                                 The vapor pressure of  species D at temperature T is  P,
                                      The gas-phase concentration of the product D will increase until the cor-
                                 responding mole fraction at which condensation begins is reached:
                     At PD = P",
                    YD =.YD,e  and                                                            (3-50)
                 condensahon starts

                                 Once saturation is reached in the gas phase,  every mole  of  D produced  con-
                                 denses. To account for the effects of  condensation on the concentrations of  the
                                 reacting species, we now write two columns for the number of moles (or irnolar
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