Page 36 - Design of Simple and Robust Process Plants
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1.11 Overall Example of Process Design  19
                 is the opening of the reactor, which brings operators into direct contact with chemi-
                 cals and introduces air into the reactor vessel ± a situation which is often undesir-
                 able. The size of the reactor was limited due to fabrication limits and the limited
                 cooling capacity for jacketed vessels. A larger vessel diameter increases the volume
                 with the cube of the diameter, while the surface area increases with the square of
                 the diameter.
                  The second generation of this batch process is shown in Figure 1.5. The reactor is
                 provided with continuous feed streams to establish a more constant heat generation
                 during the reaction feed step. To accommodate this, feed vessels are installed in
                 front of the reactor vessel. Opening of the reactor vessel is avoided by adding the
                 ingredients into harmless feed systems, or separate dosing systems are installed to
                 supply the additives. Following the reactor in this example, a post reactor is applied,
                 and de-volatilizing and cooling is carried out in separate vessels. The product is
                 intermediately stored in lot tanks to equalize the product, followed by storage. The
                 flowsheet represents a large increase in capacity by providing additional equipment
                 where the feed preparation and treatment steps are carried out, while the process is
                 automated. The additional equipment was in general justified based on incremental
                 economics. The reactor vessel was reserved for the reaction alone. Larger reactor
                 vessels could be applied (which by that time could be fabricated) due to the
                 improved control of the heat generation. Two reactor systems are shown to cover the
                 increased demand.
                   In the third-generation process, feed is applied directly to the reactor vessel, while
                 the reactor size is increased by the application of a reflux condenser, though it still


                                    Condensor Vent condensor
                  Water
                  Additives                                      Vent
                                                                recovery


                                 ~~~~~~~~~~~~~~
                   H.C. 1 feed         cooling/
                                        heating
                   H.C. 2 feed



                  Feed / Dosing Tanks Con-Add batch reactor Post reactor  Devolatization  Cooling






                    Floating storage  Additives  Basic product tanks  Filter
                 Fig. 1.6. Third-generation flowsheet of continuously added
                 batch reactor system with refluxing condensor and floating
                 storage.
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