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240                             Collection and Analysis of  Rate Data   Chap. 5

                        1.4 mrnHg/min.  By  various  plotting  or  numerical  analysis  techniques  relating
                        - yA0 to C,,   , we can obtain the appropriate rate law. If the rate law is in the form
                                                    - TAO  = kcio

                        the slope of the plot of  In (-   versus In C,,  will give the reaction order a.
                                                 i",,)

                          Example 5-3  Method of Initial Rates in Solid-Liquid Dissolution Kinetics

                           The dissolution of dolomite, calcium magnesium carbonate, in hydrochloric acid is
                          a reaction of particular importance in the acid stimulation of dolomite oil reservoirs:
                          The oil is contained in pore space of the carbonate material and must flow through
                          the small pores to reach the well bore. In matrix stimulation, HC1 is injected into a
                          well bore to dissolve the porous carbonate matrix. By dissolving the solid carbonate
                          the pores will increase in size, and the oil and gas will be able to flow out at faster
                          rates, thereby increasing the productivity of the welL5 The dissolution reaction is
                                   4HC: + CaMg(C0,),+Mg2+  + Ca2+ + 4C1- + 2C0, + 2H20

                          The concentration of  HCl at various times was determined from atomic absorption
                          spectrophotometer measurements of the calcium and magnesium ions.
            An important       Determine the reaction order with respect to HC1 from the data presented in
              reaction for   Figure E5-3.1 for this batch reaction. Assume that the rate law is in the form given
        enhancement of oil   by Equation (5-1) and that the combined rate law and mole balance for HC1 can be
          flow in carbonate
               reservoirs   given by Equation (5-6).

                                            Run 1                            Run 2
                              4.0000

                              3.9990


                           E)  3.9980
                           0
                              3.9970


                                   0     2    4'6       8            0    2    4    6    8
                                           t  (rninl                         t  (mid
                                             (01                               (b)
                                            Figure E5-3.1  Concentration-time data.

                          Solution
                          Evaluating  ,he mole balance on a constant-volume batch reactor at tiilie t = 0 gives

                                                                                    (E5;3:  1)



                         K. Lund, H. S. Fogler, and C. C. McCune, Chem. Eng. Sci., 28, 691 (1973).
                         M. Hoefner and H. S. Fogler, AZChE Journal, 34(1), 45 (1988).
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