Page 19 - 81Sulfonation-Sulfation Processing Technology for Anionic Surfactant Manufacture_opt
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286                                               Advances in Chemical Engineering

            et al., 2005), and amount sulfur trioxide in the gas phase (SO 3/N 2), finally the temperature
            of the process.  This  mathematical  model  permits  to  calculate the  profiles  of  interfacial
            liquid  temperature,  liquid  film  density,  liquid  viscosity  for any  column height  and
            longitudinal profiles of conversion. The proposed model may be suitable for use in design
            and  operation  of  industrial  film  reactors. To  ensure  convergence  of  the  system  of
            equations then transformation of the equations proposed by Agrawal & Peckover (1980)
            was  chosen  following  the same development  by  Talens  (1999). The set  of equations
            resulting  from  the mass,  momentum  and  heat  transfer is  solved  numerically.  Figure 20
            shows schematic view from the top of a reactor: the liquid is evenly distributed around
            the wall, and the gas mixture is injected through the center of the column. The interfacial
            temperature is  affected  by  the SO 3  amount  in the gas  mix. It  is  clear an increase of
            interface temperature result  of the SO 3  excess  in the gas  flow. The temperature of  the
            reagents  is  a key  control variable  to  avoid  undesirable side  impact  that  damage  the
            product mainly by strong coloration.































            Fig. 20. An example of interfacial temperature profiles fall in the reactor longitudinal
            Other example of the results provided by the model for longitudinal conversion profile from
            top of the reactor (expressed as percentage of active matter) is shown in Figure 21(a). The
            input values of the model are: SO 3/N 2 percentage at 5%, SO 3/methyl stearate mole ratio at
            1; T G, T L, and T w at 343 K, 333 K and 313 K, respectively. This figure shows schematically the
            fast conversion region at the top of the reactor (associated with gas phase control) and slow
            conversion region at  the bottom  (linked  with  liquid  phase control). The  washing  active
            substance was determinate using a two titration technique with Hyamine 1622 as the titrant
            reagent and methylene blue as indicator (Tsubochi et al., 1979; Milwdsky & Gabriel, 1982;





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