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360                                        12  Carbon Capture and Storage

              Although it is only estimation, the comparison does show that the oxyfuel
            combustion flame temperature is higher than that of conventional combustion with
            air. As a result, the boiler of the oxyfuel combustion process requires special
            materials that can survive extreme temperature.
               Another concern of the oxyfuel combustion process with sulfur containing fuels
            is the high SO x concentration without the dilution of nitrogen, resulting in high
            corrosion on the ducts. Extra costs are associated with concentrated oxygen pro-
            duction by costly air separation units.
              The benefit is a simple process for carbon capture after combustion. Without
            nitrogen and NO x in the flue gas, it contains mainly H 2 O and CO 2 . After the
            removal of soot and SO 2 , if any, CO 2 can be readily separated from water vapor by
            condensation in a cooler. This highly concentrated CO 2 is ready for transportation
            and storage.



            12.4.2.2 Chemical Looping Combustion

            Similar to oxyfuel combustion, chemical-looping combustion is an emerging
            combustion process that is attractive for the benefit of carbon capture. This idea was
            first introduced by Lewis and Gilliland [38] as a way to produce pure CO 2 from
            fossil fuels. Thirty years later, Ishida et al. [33] proposed the use of chemical-
            looping combustion for power generation with climate mitigation. Figure 12.3
            shows an example schematic diagram of chemical-looping combustion based on
            circulating fluidized bed principle. Most of the state of the art focuses on gaseous
            fuels reacting with oxygen carrier. Similar principles can be applied to the oxidation
            of the vapors of liquid fuels and volatiles released from solid fuels.
              The combustion in the fuel reactor takes place following different reaction steps.
            The oxygen-needed is released from the oxygen-carrier (Me x O y ) at high
            temperature.


                                  2Me x O y $ 2Me x O y 1 þ O 2         ð12:16Þ


            Fig. 12.3 Schematic diagram
            of the chemical looping
            combustion
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