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11.5  LIQUID-PHASE PROCESSES

            This is one of the most commonly used processes for acid gas treatment.
            Chemical solvents are used in the form of aqueous solution to react
            with H 2 SandCO 2 reversibly and form products which can be regenera-
            ted by a change of temperature or pressure or both. Physical solvents
            can be utilized to selectively remove sulfur compounds. They are
            regenerated at ambient temperature by reducing the pressure. A
            combination of physical and chemical solvents can be used. A comparison
            of chemical solvents (amines, carbonates) and physical solvents is shown
            in Table 2.

            Table 2  Comparison of Chemical and Physical Processes
                                   Chemical adsorption
                                                                  Physical
            Feature      Amine processes   Carbonate processes   absorption
            Absorbents   MEA, DEA,       K 2 CO 3 ,K 2 CO 3 þ MEA  Selexol, Purisol,
                           DGA, MDEA     K 2 CO 3 þDEA          Rectisol
                                         K 2 CO 3 þarsenic trioxide
            Operating    Insensitive to  > 200                250–1000
              pressure (psi)  pressure
            Operating    100–400         200–250              Ambient
              temperature                                       temperature
              ( F)

            Recovery of  Reboiled        Stripping            Flashing, reboiled,
              absorbents   stripping                            or stream
                                                                stripping
            Utility cost  High           Medium               Low/medium
            Selectivity  Selective for some  May be selective  Selective for H 2 S
              H 2 S, CO 2  amines (MDEA)
            Effect of O 2  Formation of   None                 Sulfur
              in the feed  degradation                          precipitation
                           products                             at low
                                                                temperature
            COS and CS 2  MEA: not       Converted to CO 2    Removed
              removal      removed         and H 2 S
                         DEA: slightly     and removed
                           removed
                         DGA: removed
            Operating    Solution        Column instability;  Absorption of
              problems     degradation;    erosion; corrosion   heavy
                           foaming;                             hydrocarbons
                           corrosion







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