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 Encyclopedia of Physical Science and Technology  EN001H-01  May 7, 2001  16:18






               4                                                                           Absorption (Chemical Engineering)


               TABLE I (continued)
                Type of plant   Feed gas          Solutes       Solvent   Commercial purpose    Stripping practice

               Ethylene oxide,  Reactor effluent  Ethylene oxide  Water  Ethylene oxide recovery  Stripping is practiced
                 glycol                                                                        to recover ethylene
                                                                                               oxide from the solution
               Ketones from  Hydrogen, ketones  Ketones         Water   Ketone–hydrogen separation  Stripping is practiced
                 alcohol                                                                       to recover ketones
                                                                                               from the solution
               Maleic anhydride  Reactor effluent  Maleic anhydride separation  Water  Maleic anhydride  Stripping is practiced
                                                                          from reactor gases   to remove water from
                                                                                               the maleic acid formed
                                                                                               in the absorption
                                                                                               process, converting it
                                                                                               back to maleic anhydride
               Isoprene      Reactor effluent  Isoprene, C 4 ’s, C 5 ’s  Heavy oil  Separation of C 4 ’s, C 5 ’s,  Stripping is practiced
                                                                          and isoprene from    to recover the solute
                                                                          light gases          and regenerate the
                                                                                               oil for recycling to
                                                                                               the absorbent
               Urea          Reactor effluent  CO 2 ,NH 3        Water   Formation of ammoniumn  Stripping not practiced
                                                                          carbonate solution,
                                                                          which is recycled
                                                                          to the reactor



               of the absorber and flows downward through the internals.  solute-free lean gas, and bottom product is the rich sol-
               Rich gas enters at the bottom of the absorber and flows  vent, which contains the absorbed solute. The rich solvent
               upward through the internals. The liquid and gas are con-  then flows to the stripper where the solute is stripped from
               tacted at the absorber internals, and the solute is absorbed  the rich solvent, this operation being at a higher tempera-
               by the solvent. Overhead product from the absorber is the  ture and/or lower pressure than maintained in the absorber.
                                                                 The solute leaves the stripper as the overhead product, and
                                                                 the solute-free lean solvent leaves the stripper bottom and
                                                                 is recycled to the absorber.


                                                                 II. PRINCIPLES OF ABSORPTION

                                                                 The important fundamental physical principles in absorp-
                                                                 tion are solubility and mass transfer. When a chemical
                                                                 reaction is involved, the principles of reaction equilibria
                                                                 and reaction kinetics are also important.

                                                                 A. Gas Solubility
                                                                 At equilibrium, the fugacity of a component in the gas
                                                                 is equal to the fugacity of the same component in the
                                                                 liquid. This thermodynamic criterion defines the relation-
                                                                 ship between the equilibrium concentration of a compo-
                                                                 nent in the gas and its concentration in the liquid. The
                                                                 quantity of gas dissolved in a given quantity of solvent
                                                                 at equilibrium conditions is often referred to as the gas
                                                                 solubility.
                                                                   Gas solubility data are available from handbooks and
                                                                 various compendia and often show solubility as a function
                FIGURE 1 Typical schematic absorber–stripper flow diagram.  of gas composition, temperature and pressure. A typical
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