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carbonate solution exits from the bottom of the absorbed and is flashed in

            the stripper, which operates at 245 F and atmospheric pressure, where acid
            gases are driven off. The lean carbonate solution is pumped back to the
            absorber.
                 The strength of the potassium carbonate solution is limited by the
            solubility of potassium bicarbonate (KHCO 3 ) in the rich stream. The high
            temperature of the system increases KHCO 3 solubility, but the reaction
            with CO 2 produces 2 mol of KHCO 3 per mole of K 2 CO 3 reacted. For this
            reason, KHCO 3 in the rich stream limits the lean solution of K 2 CO 3
            concentration to 20–35% (wt).


            11.5.3  Physical Solvent Processes
            Organic liquid (solvents) are used in these processes to absorb H 2 S
            (usually) preferentially over CO 2 at high pressure and low temperatures.
            Regeneration is carried out by releasing the pressure to the atmosphere
            and sometimes in vacuum with no heat. If we apply Henry’s law,
                 P i ¼ HX i
            or

                     Y i
                 X i ¼  P                                                ð14Þ
                     H
            This implies that acid gas absorbed in liquid phase (X i ) is proportional to
            its gas mole fraction (Y i ) and inversely to Henry’s constant (which is
            constant for a given temperature). Much more importantly, the solubility
            is proportional to the total gas pressure (P). This means that at high
            pressure, acid gases will dissolve in solvents, and as the pressure is
            released, the solvent can be regenerated.
                 The properties of four of the important solvents used in natural gas
            processing are given in Table 4.

            Fluor Process
                                                                     þ
            This process uses propylene carbonate to remove CO 2 ,H 2 S, C ,COS,
                                                                     2
            CS 2 , and H 2 O from natural gas. Thus, in one step, the natural gas can be
            sweetened and dehydrated.
                 Figure 8 shows a typical process flowsheet with regeneration
            consisting of three flash drums. The first flash drum gas containing mostly
            hydrocarbons is compressed and recycled. The second flash drum derives
            expansion turbine. The third flash contains mainly acid gases. The process
            is used to remove the bulk CO 2 down to 3%.






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