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364                                        12  Carbon Capture and Storage

            Fig. 12.4 Schematic diagram
            of pressure swing adsorption
            process




















            for moisture removal. Advances in pressured swing adsorption can be found in the
            state of the art provided by Grande [24]. A pressure swing adsorption (PSA)
            process has at least two columns, when one is working on CO 2 adsorption from the
            high pressure gas, the used sorbent in other column is regenerated at low pressure.
            A simple PSA process for CO 2 capture is shown in Fig. 12.4.




            12.5.2 Chemical Adsorbents

            Chemical adsorption at high temperature (400–600 °C) has a potential for pre-
            combustion CO 2 capture and hydrogen production. High temperature sorbent can
            be employed for carbon separation without temperature quenching and conse-
            quently do not comprise much with overall energy efficiency. The working prin-
            ciples are similar to those of calcium based adsorption.



            12.5.2.1 Calcium-Based Adsorbent

            CaO is one of the oldest sorbent for CO 2 capture by chemical adsorption. Calcium
            oxide reacts with CO 2 at high temperatures to produce carbonates:

                                                                        ð12:24Þ
                                  CaO sðÞ þ CO 2 $ CaCO 3 sðÞ
            where (s) stands for solid state. The forward reaction takes place at about
            600–800 °C, and the backward reaction at higher temperature (>870 °C) may result
            in sorbent regeneration by decarbonation and releasing CO 2 .
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