Performance of a silica-polyethyleneimine adsorbent for post-combustion CO2 capture on a 100 kg scale in a fluidized bed continuous unit

• Published in: Chemical engineering journal (Lausanne, Switzerland : 1996) Vol. 407; p. 127209
• Main Authors: Kim, Jae-Young, Woo, Je-Min, Jo, Sung-Ho, Kim, Hyunuk, Lee, Seung-Yong, Yi, Chang-Keun, Moon, Jong-Ho, Nam, Hyungseok, Won, Yooseob, Stevens, Lee A., Sun, Chenggong, Liu, Hao, Liu, Jingjing, Snape, Colin E., Park, Young Cheol
• Format: Journal Article
• Language: English
• Published: Elsevier B.V 01.03.2021
• Subjects: 100 kg scale fluidized bed continuous unit; CO2 purity; Oxidative degradation; Post-combustion CO2 capture; Silica-PEI adsorbent; Post-combustion CO2 capture; 100 kg scale fluidized bed continuous unit; Silica-PEI adsorbent; CO2 purity; Oxidative degradation
• ISSN: 1385-8947; 1873-3212
• DOI: 10.1016/j.cej.2020.127209

•Silica-PEI adsorbent has been evaluated on a 100 kg scale in 150 h continuous test.•Optimal gas velocity for adsorbent in a bubbling fluidized-bed reactor was 5.1 cm/s.•≥90% CO2 removal efficiency was achieved with ≥7.5% dynamic sorption capacity.•Working capacity decreased with an increase of CO2 partial pressure in desorber.•CO2 sorption performance of the adsorbents decreased as testing time increased. Polyethyleneimine (PEI)/silica adsorbents have been considered as a promising candidate for post-combustion CO2 capture, but the limited process study has been performed on a pilot-scale unit. Herein we report the 150 h continuous test results using a 100 kg sample of silica-PEI on a fluidized bed continuous unit. The CO2 removal efficiency and dynamic sorption capacity were evaluated continuously by changing a number of variables. For the sorption reactor, the changing variables were inlet H2O concentrations of 0–8.3 vol%, inlet CO2 concentrations of 12.0–21.5 vol%, bed temperatures of 50–70 °C and the bed differential pressures of 176–370 mmH2O. For the desorption reactor operated at the bed temperature of 129–130 °C, inlet H2O concentrations of 8.0–13.5 vol%, inlet CO2 concentrations of 14.6–81.2 vol% and bed differential pressures of 430–580 mmH2O were used. During continuous operation, CO2 removal efficiencies of over 90% were achieved with dynamic sorption capacities of 7.5 wt%. Solid sample collected during continuous operation were analyzed by TGA and 13C NMR to identity the decrease of CO2 adsorption capacity and the extent of thermo-oxidative side reactions. Slow oxidative degradation of the silica-PEI occurred because the transporting adsorbent was exposure to the non-humidified air in the solid transport system.