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Air injection                                                407


              experimental data, along with the starting temperature and the content of
              exotherms. To reach adiabatic conditions, an oil sample is usually put in a
              “close” ARC system. But a “flowing” type of ARC testing system is also
              possible with the oil sample under a high air purge and at a quasiadiabatic
              operation (Yannimaras and Tiffin, 1995). ARC is similar to DSC or TG
              except that reactions can be performed at a high pressure in ARC.


                   13.3 Kinetic parameters

                   Oxidation reaction rates are described commonly using the Arrhenius
              type of equation which includes several kinetic parameters: activation energy,
              frequency factor and reaction order. These kinetic parameters are obtained
              through thermogravimetry (TG) and Differential scanning calorimetry
              (DSC), accelerating rate calorimeter (ARC), and small batch reactor (SBR).
              Example methods to obtain kinetic parameters using TG and DSC are
              presented next.

              13.3.1 Thermogravimetric analysis (TGA)
              Oxidation is a thermal decomposition process which needs kinetic parameters
              to describe it. One of the classic methods is based on the Arrhenius method to
              estimate the kinetic parameters from thermogravimetric tests or thermo-
              gravimetric analysis (TGA) (Coats and Redfern, 1964). The time-derivative
              thermogravimetric (DTG) data are readily available in TG equipment and
              sometimes used together with TG data. A TG test is used to measure the
              mass loss of a substance as the temperature is increased. It is described by
              the following equation:

                                     dm t
                                                                         (13.1)
                                      dt  ¼ kf ðm; C o ; .Þ
              where f(m,C o , .) is a function of the mass m t remaining at time t, oxidation
              concentration, etc., k is the temperature-dependent rate constant, (m/t),
              which is described by the Arrhenius equation:


                                                 E
                                                 RT
                                        k ¼ Ae                           (13.2)
                                                              1     1
              where A is the preexponential or frequency factor, [t ], (s ). E is the
                                                            2
                                                          2
              activation energy of the decomposition reaction, [L /t ], (kJ/mol). R is the
                                   2
                                       2
              universal gas constant, [L /Tt ], (kJ/mol K). T is the absolute temperature,
              [T], (K).
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