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Figure 23.  SO 3 Absorber System


                                          SO  GAS
                                             3
                                           FROM
                                         GAS PLANT

                                          PROCESS
                                           WATER


                                                                  ABSORBER
                                                                    TOWER
                                                                             EFFLUENT
                                                                               GAS


                                                                             SEPARATOR
                                          CWS                                   TANK
                                          CWR





                                                                                98%
                                                                           SULFURIC ACID


                   Several types of commercial sulfonators are available.  In broad classifications they are
                   film reactors [6, 7, 8, 9] , including the Chemithon Annular Falling Film Reactor [10, 11, 12] , the
                   Ballestra [13] , IIT and Siprec multitube film reactors; the Chemithon dispersed phase or jet
                   reactors [14, 15, 16] ; and stirred tank or cascade type reactors [17] .  Film reactors are the most
                   common in detergent processing for consumer products, especially to produce cosmetic
                   quality materials from oleo chemical feedstocks.  In a film reactor, the organic feedstock
                   is extruded onto the wall of the reactor (reaction surface) as a continuous film.  Organic
                   feed rate to the reactor vessel is measured by a highly accurate mass flow meter and
                   controlled by a variable speed driven gear pump.  The proper organic feed rate is based
                   on the preset sulfur-to-organic mole ratio.  The SO , diluted with very dry air, flows over
                                                                    3
                   the film of organic material.  The SO  diffuses into the organic film and reacts to form a
                                                       3
                   sulfonic acid.  In almost all commercial reactors both the organic and SO  flow
                                                                                         3
                   concurrently from the top of the reactor to the bottom.  The heat of reaction is removed
                   by cooling water which flows through cooling jackets underneath the reaction surface of
                   the reactor.




                   Page 24 of 36                                                  © 1997 The Chemithon Corporation
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