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availability, etc.) and economically viable (higher capital cost of building a bigger CO2 capture system as well as an auxiliary boiler, higher O&M costs etc.). In the present version of IECM, this configuration option is not included. Figure 3. CO2 Capture Plant Configuration Options a) Reference base plant b) Capture plant with internal derating c) Capture plant with an auxiliary boiler and a secondary steam turbine In terms of the configuration of the CO2 capture system shown in Figure 3, the user can make the following choices as well Direct contact cooler: The default setting in IECM chooses to include a DCC to cool the flue gas before it enters the amine system. The temperature of the flue gas affects the absorption reaction (absorption of CO2 in MEA sorbent is an exothermic process favored by lower temperatures). Also, the volumetric flow rate of the flue gas stream, which is a key determinant of the sizes of various equipments (direct contact cooler, flue gas blower, absorber), is directly related to the flue gas temperature. Hence lower flue gas temperature is desired. The typically acceptable range of flue gas temperature is about 50-60 oC. If the flue gas is coming from wet sulfur scrubber, additional DCC may not be required. But in case of flue gas from NG-fired boiler, which often does not pass through a sulfur scrubber, DCC is a must. Choice of sorbent: At this time, MEA is the default sorbent used in the system and the nominal values of various parameters are based on a process simulation model that uses MEA. As always, the users can Integrated Environmental Control Model - Technical Documentation • 8PDF Image | Amine Based CO2 Capture
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