Page 75 - The engineering of chemical reactions
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Chemical  Equilibrium  59
                             (Pj),  mole fraction (xj),  and concentration (Cj).  For these units the standard state is defined
                             as unit activity aj,  which is typically Pj  = 1 atm and 298 K, or Xj =  1 for pure liquid at 1
                             atm and 298 K, or Cj  = 1 mole/liter at 298 K, respectively. Students have seen the first two
                             of these for gases and liquids in thermodynamics. We will use concentration units wherever
                             possible in this course, and the natural standard state would be a 1 molar solution. However,
                             data are usually not available in this standard state, and therefore to calculate equilibrium
                             composition at any temperature and pressure, one usually does the calculation with  Pj  or
                             Xj  and then converts to Cj .
                                  As  zfinal  remark on the importance and use of thermodynamics in chemical reactors,
                             we note that the preceding equations no longer need be solved in practice because thermo-
                             dynamics computer programs and databases allow one to compute all these quantities by
                             simply listing the molecules and conditions into the computer programs. The data in Table 2-
                             2 were calculated using CHEMEQ from Sandler’s thermodynamics text, and sophisticated
                             chemical process programs such as ASPEN contain databases for most of the complex
                             molecules and conditions that one might encounter in industrial practice.
                                  The variations in  KT  with temperature are shown in Figure 2-l 1 for the reactions in

                             Table 2-2. These should be straight lines when plotted as log  KT  versus  l/ T  if A  HR   is
                             independent of temperature, and the curves show that this approximation is accurate for all
                             these reaction systems.



                                  T WI                                     T WI
                       2000   1000800  500 400   300            2000   1000800  500 400   300


                 10'5






             K                                        K   10'0
              eq                                       eq

                                                           100
                                                                   \

                                                                  1/2N,+3/2H,+NH,
                                                                C,H,+H,O*C,H,OH  trark-C,H8#cis2-C,H,
                 .-                                               I   I    I   I    I   I
                    0   0.5  1   1.5  2   2.5  3   3.5           0.5  1   1.5  2   2.5  3   : 5
                                  1000                                     1000
                                  T W)                                     T  (K)
             Figure  2-11  Plots of equilibrium constant KT versus temperature for several chemical reactions we will consider in this text.
             All these reactions give nearly straight lines when plotted as log KT versus l/ 7’.  Exothermic reactions have large KT at low T,
             while endothermic reactions have large  KT  at high T.
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