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waste acid must be separated from the reaction mixture and subsequently disposed.  In
                   North America, the expense of disposing the "spent" sulfuric acid has become so high
                   that the process economics are now questionable.

                   Sulfonation with sulfuric acid is a special case of oleum sulfonation. Because the
                   sulfonation reaction stops when the acid concentration in the reaction mixture drops to
                   less than approximately 90%, sulfonation of detergent feedstocks with sulfuric acid is not
                   normally practiced.  Today sulfuric acid sulfonation is principally used for production of
                   hydrotropes by azeotropic reaction with benzene, toluene or xylene.  In this special
                   process, the water formed during the reaction is removed by azeotropic distillation of the
                   water and unreacted feedstock.  The water is then separated from the immiscible organic
                   feedstock which is returned to the reaction vessel.  Because water is removed, the
                   reaction may continue to completion.


                   The air/SO  sulfonation process is a direct process in which SO  gas is diluted with very
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                              3
                   dry air and reacted directly with the organic feedstock.  The source of the SO  gas may be
                                                                                             3
                   either liquid SO  or SO  produced by burning sulfur.  As shown in Figure 8, the reaction
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                                  3
                   of gaseous SO  with organic is rapid and stoichiometric.  It is complicated by the
                                 3
                   possibility of side reactions and therefore tight process control is essential.  The cost for
                   liquid SO  is US$0.09 per pound of reactive SO ; while SO  from sulfur burning is
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                            3
                                                                 3
                   US$0.02 per pound of reactive SO .  The air/SO  sulfonation process is the lowest SO
                                                    3
                                                                                                      3
                                                                 3
                   cost of any sulfonation process and is extremely versatile, producing very high quality
                   products.  However, it is a continuous process best suited to large production volumes.
                   In addition, it requires expensive precision equipment and highly trained operating
                   personnel.
                   Figure 8.  Air / SO 3
                             SO   +  CH - (CH )  - CH - (O - CH - CH ) - OH
                                               2 10
                                                        2
                                3
                                        3
                                                                   2
                                                                         2 3
                            Sulfur            Ethoxylated lauryl alcohol
                           trioxide
                                                                            O
                                                                                  –
                                CH - (CH )  - CH - (O - CH - CH ) - O - S - O    H     +
                                          2 10
                                                              2
                                                   2
                                                                    2 3
                                   3
                                                                            O
                                       Ethoxylated lauryl alcohol sulfuric acid



                   Page 6 of 36                                                   © 1997 The Chemithon Corporation
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