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12.6  CO 2 Separation by Absorption                             367

            12.6.2 Amine-Based Chemical Absorption

            Chemical absorption is suitable for CO 2 capture at low pressure and low temper-
            ature. The sorbents used for chemical absorption include carbonate-based, sodium
            hydroxide-based, aqueous ammonia-based, and amine-based sorbents.
              Amine-based CO 2 absorption is a relatively mature technology used in the
            ammonia process, steam reforming process, and the natural gas sweetening process.
            Amines are ammonia-derived organic compounds when one or more hydrogen
            atom(s) of ammonia are replaced with organic substituents. Amines are classified as
            primary, secondary, and tertiary amines based on the number of replaced hydrogen
            atoms.
              The choice of amine for CO 2 absorption depends on three key factors: rate of
            reaction, regeneration energy, and loading capacity. The ideal solvent is characterized
            with a great rate of reaction, low regeneration energy, and great loading capacity.
            However, none of the alkanolamines meets all these three requirements. In general,
            the rate of reaction follows the order of primary > secondary > tertiary; the order is
            reversed for regeneration energy and loading capacity [35]. Ethanolamine (C 2 H 7 NO
            or 2R-NH 2 ), also called 2-aminoethanol or monoethanolamine (MEA) is the most
            commonly used amine for CO 2 absorption. It is a primary amine, and a alcohol too.
              Among all the amines tested, MEA showed its high reactivity with CO 2 , and is
            predominantly used for CO 2 capture in the industry. Aqueous amine solutions are
            bases and the pKa values of typical alkanolamines are listed in Table 12.5. Thereby,
            amines can react with not only CO 2 but also other acidic gases like SO 2 and NO 2 at
            great rates of reactions. Therefore, SO 2 and NO 2 have to be effectively removed
            first before CO 2 absorption if it is to be used for post-combustion carbon capture. It
            also reduces the contamination to the regenerated solvent and recovered CO 2 .


            12.6.2.1 Kinetics of Amine-CO 2 Reactions

            As the most popular CO 2 absorbent, the kinetics of CO 2 reaction with alkanolamines
            deserves an in-depth discussion. The reaction of CO 2 with primary and secondary



            Table 12.5 pKa values of base amines at 298 K
            Amine                                                          pKa
            MEA                      Monoethanolamine                      9.50
            DEA                      Diethanolamine                        8.88
            DIPA                     Diisopropanolamine                    8.80
            TEA                      Triethanolamine                       7.76
            MDEA                     Methyldiethanolamine                  8.57
            AMP                      2-Amino-2-methyl propanol             9.70
            DEMEA                    Diethylmonoethanolamine               9.82
            Source:[54]
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