Page 440 - Enhanced Oil Recovery in Shale and Tight Reservoirs
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408                            Enhanced Oil Recovery in Shale and Tight Reservoirs


             The function f(m,C o , .) describes how the reaction (mass loss here)
          depends on the available mass, oxygen concentration, etc. If the reaction
          is not dependent on any of those parameters, the function is essentially
          one. The reaction is zero-order. If the reaction depends on one of those
                                                              n
                          n
          parameters, e.g., C , the function becomes a function of C which means
                          o                                  o
          the nth order of reaction of C o . Make sure the units are consistent.
             For the purpose of simplifying the explanation, it is assumed the reaction
          order is zero. By combining Eqs. (13.1) and (13.2):

                                               E
                                    dm t       RT
                                       ¼ Ae                          (13.3)
                                    dt
                                                               dT
                                                               dt
             For nonisothermal TG tests with a linear heating rate b ¼  , Eq. (13.3)
          can be written as

                                               E
                                    dm t  A    RT
                                       ¼ e                           (13.4)
                                    dT    b
             Taking the logarithm of both sides of Eq. (13.4), it becomes

                                  dm t       A     E
                               ln      ¼ ln                          (13.5)
                                  dT         b    RT

          When y ¼ ln  dm t                     1  for the experimental data, a
                        dT  is plotted versus x ¼  T
          straight line is obtained that will have a slope of E/R and the intercept of
          ln(A/b). The value of activation energy E and frequency factor A can be
          obtained from the slope and the intercept of the linear fit line, respectively.
          During a TG test, mass loss versus temperature is measured.
             Note that as the temperature is increased, oil may be distilled, and the
          mass will be lost under air or oxygen purge. In other words, the mass loss
          is not totally by oxidation. Therefore, it is suggested the TG test under
          nitrogen purge should be carried out as a base line. Fig. 13.5 is an example
          of TG tests under air and nitrogen purge (Huang et al., 2016a). First, note
          that the two curves under air and nitrogen purge were not two straight lines
          in the whole temperature range as Eq. (13.5) suggests, indicating the
          reactions were not zero order. The figure shows that the two oil mass curves
          overlapped before 192 C, indicating a distillation-dominant process. After

          192 C, oil weight sharply decreased. At around 348 C, weight remaining


          for the oil sample under air purging was around 9% and 15% for nitrogen
          purging. The difference of weight remaining at a particular temperature
          was owing to oxidation reactions at low temperature stages. Some of the
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