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58   Gas Purgcation




                     PURIFIED              SOLUTION  =  1  1-
                                        ,ETHANOLAMINE
                       GAS                                    STEAM



                                                                               ACID GAS
                                                                              TO DISPOSAL













                       Figure 2-10. Basic flow scheme for alkanolamine acid-gas removal processes.


                    more concentrated. Generally, all of this water, or a major portion of it, is fed back to the top
                    of  the stripping column at a point above the rich-solution feed and serves to absorb and
                    return amine vapors carried by the acid gas stream.
                      Many modifications to the basic flow scheme have been proposed to reduce energy con-
                    sumption or equipment costs. For example, power recovery turbines are sometimes used on
                    large, high-pressure plants to capture some of  the energy available when the pressure is
                    reduced on the rich solution. A minor modification aimed at reducing absorber column cost
                    is the use of  several lean amine feed points. In an arrangement described by Polasek et al.
                    (1990), most of the lean solution is fed near the midpoint of the absorber to remove the bulk
                    of the acid gas in the lower portion of the unit. Only a small stream of lean solution is need-
                    ed for final clean-up of the gas in the top portion of  the absorber, which can therefore be
                    smaller in diameter.
                      A modification that has been used successfully to increase the acid gas loading of the rich
                    amine (and thereby decrease the required solution flow rate) is the installation of a side cool-
                    er (or intercooler) to reduce the temperature inside the absorber. The concept has proved par-
                    ticularly useful for DGA plants operating in Saudi Arabia where air cooling is used (Huval
                    and van de Venne,  1981). The optimum location for a side cooler is reported to be the point
                    where half the absorption occurs above and half below the cooler, which results in a location
                    near the bottom of the column (Thompson and King, 1987).
                    Water Wash for Amine Recovery

                      The simplest modification of  the flow system in Figure 2-10  is the inclusion of  a water
                    wash at the top of the absorber to reduce losses of  amine with the purified gas. If acid gas
                    condensate from the regenerator reflux drum is used for this purpose, no draw-off  tray is
                    required because it is necessary to readmit this water to the system at some point. It should
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