Analysis of Operation Conditions of Ca(OH)(2) Entrained Carbonator Reactors for CO(2) Capture in Backup Power Plants

[Image: see text] The share of renewables in the energy sector is increasing, and energy storage and backup power combustion systems to cover the periods of time with low renewable energy production are becoming increasingly needed. Flexible calcium looping configurations based on the storage of solids are a promising alternative to capture the CO(2) produced in such backup combustion systems. The use of Ca(OH)(2) instead of CaO is better suited to these applications due to the faster reaction kinetics and higher carbonation conversions as Ca(OH)(2) in powder form can achieve conversions of up to 0.7 in just a few seconds at temperatures of 550–650 °C. To take advantage of these fast reaction kinetics, compact carbonator reactors with short gas–solid contact times (i.e., a few seconds) can be designed. However, the low enthalpy of the carbonation reaction of Ca(OH)(2) makes it challenging to find the optimum conditions which maximize the CO(2) capture efficiency. In this work, a basic entrained reactor with recent experimental reaction kinetics has been used to determine suitable operational windows for this kind of carbonator. CO(2) capture efficiencies above 90% can be achieved for flue gases with low CO(2) concentrations (4%(v) CO(2)) when they are fed into the carbonator at temperatures of around 500–600 °C while maintaining low F(Ca)/F(CO2) ratios (<2) and feeding the sorbent at ambient temperature. When capturing from a flue gas with a higher CO(2) concentration (14%(v) CO(2)), the sorbent needs to be fed at higher temperatures to effectively capture CO(2) in short contact times (i.e., 6 s).