Page 477 - Enhanced Oil Recovery in Shale and Tight Reservoirs
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Air injection                                                441


              does show that heat loss is reduced in the reservoir. However, with such low
              temperature increase, spontaneous ignition cannot occur in the reservoir.
                 Huang and Sheng (2018) also used the field model to have done sensi-
              tivity analyses, similarly to what is done for the base laboratory model. They
              found that the cumulative oils produced from air injection and nitrogen
              injection are similar; the peak temperature near the injector is less than
              150 C (the original reservoir temperature 99 C) by increasing the frequency


              factor, reducing the activation energy causes, injection of pure oxygen, or
              increasing the enthalpy. All these results indicate that spontaneous ignition
              cannot occur in the reservoir under low-temperature oxidation reactions.

              13.5.4 Delay time of spontaneous ignition
              Spontaneous ignition occurs as the heat from oxidation reactions is accumu-
              lated so that the temperature is increased to reach an ignition temperature.
              An analytical solution for the ignition delay time in days was proposed by
              Tadema and Wiejdema (1970) and then modified by Hou et al. (2011):

                   ð1   fÞr C r þ fS org r C o þ fS wc r C w þ fð1   S org   S wc Þr C g E
                                      o
                           r
                                                                        g
                                                 w
              t SI ¼                                 n
                                                   Ap
                                         RfS org Q O 2
                                                     O 2
                  ("                    #         )
                            2          3             T r
                       RT         RT          E
                             þ 2         exp
                        E          E         RT
                                                     T SI
                                                                        (13.12)
                 In the above equation, f is the effective porosity; r , r , r are the
                                                                      o
                                                                   w
                                                               r
                                                                          3
              average densities of reservoir rock, water, and oil, respectively, kg/m ; T r
              is the reservoir initial temperature, K; T SI is the spontaneous ignition
              temperature, K; C r , C o , C w , C g are the heat capacities of reservoir rock,
              oil, water, and gas, respectively, kJ/(kg$ C); S org and S wc are the residual

              oil saturation under gas drive and connate water saturation, respectively; E
                                                                   is the partial
              is the activation energy of the oxidation reaction, J/mol; p O 2
                                                                     n
                                                               1
              pressure of oxygen, kPa; A is the frequency factor, day $kPa ; R is the
              universal gas constant which equals to 8.3147 J/(mol$K); n is the reaction
                                                                       3
                           is the enthalpy of the corresponding reaction, kJ/m . Using
              order; and Q O 2
              the above analytical equation, examples of calculated time delay in ignition
              are shown in Fig. 13.23.
                 The above equation is derived based on the balance between the heat
              generated by a low-temperature oxygen-addition reaction Q O 2  $p O 2  $ A$
              expð  E=RTÞ$dt and the heat required C f $ r $dT to increase the reservoir
                                                     f
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