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In amine-based post-combustion CO2 capture, solvent loss contribute to process operation problems like corrosion, fouling, foaming as well as is responsible for economic deficit. In this work, thermal degradation of blended 3.2m DEA and 0.8m was investigated at 135°C, simulating the stripper temperature. CO2 loading of the system was varied from 0.0 to 0.4mole CO2/mole alkalinity to explore its effect...
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