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Commercial Scale Sulfonation Equipment

                   Sulfamic Acid Sulfation Equipment

                   Figure 11 illustrates the equipment used for sulfamic acid sulfation.  This batch process is
                   run in a stainless steel or glass lined, air tight, stirred tank reactor.  The reactor has
                   heating and cooling coils and provision for weighing in the organic reactant and the
                   sulfamic acid.  Before the reaction starts, air is purged from the reactor with dry nitrogen
                   and the reaction is run under a blanket of nitrogen.  The organic is weighed into the
                   reactor and a 5% molar excess of sulfamic acid is then added.  The reactor is purged and
                   blanketed with dry nitrogen to remove oxygen.  The reactants are heated to 110–160°C
                   and held at this temperature for approximately 90 minutes.  The products are then cooled
                   to 70°C and water or alcohol are added to dilute the product.  As previously mentioned,
                   an ammonium salt is the direct reaction product so no neutralization step is required.


                   Figure 11.  Sulfamic Acid Sulfation


                                                                               Solid granular
                                                                               sulfamic acid

                                                                               Scale






                                                                                Heating/
                                                                                Cooling






                                         Organic
                                          Feed
                                                                              Product

                                                                         Load cell













                   Page 10 of 36                                                  © 1997 The Chemithon Corporation
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