Page 98 - The engineering of chemical reactions
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82    Reaction Rates, the Batch Reactor, and the Real World

                       2.6 (a) The previous process was found to have an activation energy of 12  kcal/mole,  and we had
                             been operating at 40°C. What reactor volumes would we need if we can operate at  8O”C?
                          (b) This hydrolysis reaction is exothermic with  AH,  = -8 kcal/mole.  What must be the
                             average rate of cooling (in watts) during the reaction to maintain the reaction isothermal?
                          (c) If we started the batch reactor at 40°C but forgot to turn on the cooling, what would be the
                             final temperature if the reactor were adiabatic (and the vessel would withstand the pressure)?
                             Assume the heat capacity of the solution to be that of water, 1  Cal/cm3  K.
                          (d) What cautions do you recommendations regarding operation at 8O”C?
                       2.7 An aqueous ester hydrolysis reaction A  +  B  + C has k  = 0.02 min-l  and an equilibrium
                          constant of 10 with all concentrations in moles/liter.
                          (a) Starting with  CA0 = 1 mole/liter, and  C&,  = Cc0  =  0, what is the equilibrium composition?
                          (b) What is the reverse rate constant in the above reaction?
                          (c) Find  CA(I), C,(t),  and  Cc(t)  in a batch reactor for these initial conditions.

                       2.8 (a) Sketch the steps, reactions, and flow sheet by which ethylene glycol is produced from ethane
                             by the direct oxidation process.
                          (b) Ethylene glycol was made by the chlorohydrin route until the 1960s  when Union Carbide
                             and Shell Oil developed the direct oxidation process. In the chlorohydrin process hypochlor-
                             ous acid, HOCl,  is reacted with ethylene to produce ethylene chlorohydrin. Then HCl  is
                             eliminated and the product is hydrated. Sketch these reactions and the flow sheet, starting
                             from NaCI, ethane, water, air, and electricity.
                          (c) If the HCl must be disposed of by reacting it with NaOH,  how many pounds of salt must be
                             disposed of per pound of ethylene glycol produced, assuming all reaction steps have 100%
                             efficiency?
                          (d) Write out the ethane to ethylene glycol reactions in our standard notation,  c Vij Aj = 0,  i =
                             1,2,.  . ,  R.

                       2.9 Summarize the argument that all chemical energy sources are derived from solar energy. What
                          is the single chemical reaction and what is the catalyst by which all of this chemical energy is
                          produced? [Look it up in your biology text.] What is a reasonable definition of renewable and
                          nonrenewable energy sources? What is the major reaction by which  CO2  is removed from and
                          added to the biological cycle?

                      2.10 Before synthetic polymers were developed to produce fibers and sheets, your ancestors found
                           many natural sources of polymers for clothing, housing, and tools. Make a list of these divided
                           into soft materials and hard materials and into one-dimensional and two-dimensional polymers.
                           List the source, uses, and chemical composition for each. Don’t forget violin bows, guitar
                           strings, writing surfaces, and wine jugs.

                      2.11 We have a process that reacts 67% Cl&  in 02 at 10 atm to form syngas (A  HR = -8.5 kcahmole
                           CH4).
                           (a) Estimate the adiabatic reactor temperature at completion if we produce 100% syngas with
                              a feed temperature of 400°C. Assume  pC, =  i R = 7  Cal/mole  K.
                           (b) Estimate the adiabatic reactor temperature if we suddenly begin producing 100% total
                              combustion products (A  HR = - 192  kcal/mole).
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