Page 124 - Gas Purification 5E
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1 14   Gas Purijcation

                             200


















                              40

                              30



                              20
                                10            20      90   405060        80100
                                                  Ow Flowrate. MMscM
                    Figure 2-79. Approximate diameter required for baytype amine plant absoaers. (Iolan
                    and Manning, 1-


                    H2S in the treated gas leaving these trays. Therefore, in these circumstances, the H2S content
                    of the treated gas is independent of the absorber design and depends only on the lean amine
                    temperature and the amine regenemtor performance. Absorbers with 20 trays can usually
                    meet all common treated gas COz specifications; however, more than 20 trays may be
                    required if C02 in the treated gas is to be close to equilibrium with the lean amine. Therefore,
                    in applications such as synthesis gas treating, where it is advantageous to reduce the C@  con-
                    tent of  the treated gas to very low levels, absorbers containing more than 20 trays or the
                    equivalent height of packing are often specified.
                      As previously noted, in typical 20-tray absorbers, the bulk of the acid gas is absorbed in the
                    bottom half of the column, while the top portion serves to remove the last traces of acid gas and
                    reduce its concentration to the required product gas specification. With sufficient trays and
                    amine, the ultimate purity of the product gas is limited by equilibrium with the lean solution at
                    the product gas temperature. When water washing is necessary to minimize amine loss (e.g.,
                    with low-pressure MEA absorbers), two to four additional trays are commonly installed above
                    the acid gas absorption section. A high efficiency mist eliminator is recommended for the very
                    top of the absorber to minimize carryover of amine solution or water.
                      Stripping columns commonly contain 12 to 20 trays below the feed point and two to six
                    trays above the feed to capture vaporized amine. Split stream plants obviously require more
                    trays. One unit, for example, employs a total of 33 trays in the stripping column with chim-
                    ney trays at the base and at the seventeenth tray from the bottom (Bellah et al.,  1949). The
                    less volatile amines, such as DEA and MDEA, require fewer trays above the feed point to
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