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Chap. 1   Supplernentary Reading                                31
                                                   CD - ROM  MATERIAL

                                 Learning Resources
                                 1. Sturnnary Notes for Lectures  I  and 2
                                 2.  Mkb Modules
                                    A,.  Problem Solving Algorithm for Closed-Ended Problems
                                    B.  Hints for Getting Unstuck on a Problem
                                 3.  Interactive Computer Modules
                                    A,.  Quiz Shlow I
                                 4.  Solved Problems
                                    PI. CDP1-A.B Batch Reactor Calculations: A Hint of Things to Come
                                 Professional Reference Shelf
                                  I.  F’hotograph,s of  Real Reactors
                                  FAG!  [Frequently Asked Questions]- In UpdatesIFAQ icon section
                                  Additional Homework Problems
                               NOTE TO INSTRUCTORS: Additional problems (cf. those from the preceding edition) can be
                                 found in the solutions manual and on the CD-ROM. These problems could be photocopied
                                 and used to help reinforce the fundamental principles discussed in this chapter.

                                  CDl’l-AA   Calculate the time to consume 80% of species A in a constant-volume
                                            btatch reactor for a first- and a second-order reaction. (Includes Solution)
                                  CDID1-BA  Derive the differential mole balance equation for a foam reactor. [2nd
                                            Ed. P1-1oB]


                                              SUPPLEMENTARY  READING

                                 1. For further elaboration of the development of the general balance equation, see

                                     DIXON, D. C.,  Chem. Eng. Sci., 25, 337 (1970).
                                     FELDER, R. M., and R. W.  ROUSSEAU, Elementary  Principles of  Chemical Pro-
                                         cesses, 2nd ed. New York Wiley, 1986, Chap. 4.
                                     HIMMELBLAU, D. M., Basic Principles and Calculations in Chemical Engineer-
                                         ing, 6th ed. Upper Saddle River, N.J.: Prentice Hall, 1996, Chaps. 2 and 6.
                                     HOLLAND, C. D., and R. G. ANTHONY, Fundamentals of  Chemical Reaction Engi-
                                         neering, 2nd ed. Upper Saddle River, N.J.: Prentice Hall, 1989, Chap. 1.

                                 2. A detailed explanation of a number of topics in this chapter can be found in
                                     CRYNES,  EL L.,  and H.  S. FOGLER, eds., AIChE lModular Instruction Series E:
                                         Kinetics, Vols.  1  and 2. New York AIChE, 1981.
                                 3.  An excellent description of the various types of commercial reactors used in indus-
                                   try is found in Chapter 11 of
                                     WAIAS, S. M., Reaction Kinetics for C-al   Engineem New Yo&.  McGrawHill, 1959.
                                   A somewhat different discussion of the usage, advantages, and limitations of vari-
                                   ous reactor types can be found in
                                      DENBIGH, K. G., and J.  C. R. TURNER, Chemical Reactor Theory, 2nd ed. Cam-
                                         bridge: Cambridge University Press, 1971, pp.  1-10.
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