TY - JOUR
T1 - Beyond carbon capture towards resource recovery and utilization
T2 - fluidized-bed homogeneous granulation of calcium carbonate from captured CO2
AU - Huang, Yao Hui
AU - Garcia-Segura, Sergi
AU - de Luna, Mark Daniel G.
AU - Sioson, Arianne S.
AU - Lu, Ming Chun
N1 - Funding Information:
The authors would like to thank the Ministry of Science and Technology , Taiwan (Contract No. MOST-102-2221-E-041-001-MY3 ) and the Department of Science and Technology, Philippines for providing financial support for this research undertaking.
Funding Information:
The authors would like to thank the Ministry of Science and Technology, Taiwan (Contract No. MOST-102-2221-E-041-001-MY3) and the Department of Science and Technology, Philippines for providing financial support for this research undertaking.
Publisher Copyright:
© 2020
PY - 2020/7
Y1 - 2020/7
N2 - Atmospheric carbon dioxide (CO2) imbalance due to anthropogenic emissions has direct impact in climate change. Recent advancements in the mitigation of industrial CO2 emissions have been brought about by a paradigm shift from mere CO2 capture onto various adsorbents to CO2 conversion into high value products. The present study proposes a system which involves the conversion of CO2 into high purity, low moisture, compact and large CaCO3 solids through homogeneous granulation in a fluidized-bed reactor (FBR). In the present study, synthetic solutions of potassium carbonate (K2CO3) and calcium hydroxide (Ca(OH)2) were used as sources of carbonate and precipitant, respectively. The effects of the degree of supersaturation (S) as chemical loading and influx flow rate (QT) as hydraulic loading on CaCO3 granulation efficiency were investigated. In the study, S was varied from 10.2 to 10.8 and QT from 40 to 80 mL min−1 while the operating pH and calcium-is-to-carbonate molar ratio ([Ca2+]/[CO32−]) were set at 10 ± 0.2 and 1.50, respectively. Results showed that carbonate ions end product distribution had a highest carbonate granulation efficiency at [Carbonate]G of 95–96% using S of 10.6 and QT of 60 mL min−1. Characterization of the granules confirmed high purity calcium carbonate. Overall, the transformation of industrial CO2 emissions into a valuable solid product can be a significant move towards the mitigation of climate change from anthropogenic emissions.
AB - Atmospheric carbon dioxide (CO2) imbalance due to anthropogenic emissions has direct impact in climate change. Recent advancements in the mitigation of industrial CO2 emissions have been brought about by a paradigm shift from mere CO2 capture onto various adsorbents to CO2 conversion into high value products. The present study proposes a system which involves the conversion of CO2 into high purity, low moisture, compact and large CaCO3 solids through homogeneous granulation in a fluidized-bed reactor (FBR). In the present study, synthetic solutions of potassium carbonate (K2CO3) and calcium hydroxide (Ca(OH)2) were used as sources of carbonate and precipitant, respectively. The effects of the degree of supersaturation (S) as chemical loading and influx flow rate (QT) as hydraulic loading on CaCO3 granulation efficiency were investigated. In the study, S was varied from 10.2 to 10.8 and QT from 40 to 80 mL min−1 while the operating pH and calcium-is-to-carbonate molar ratio ([Ca2+]/[CO32−]) were set at 10 ± 0.2 and 1.50, respectively. Results showed that carbonate ions end product distribution had a highest carbonate granulation efficiency at [Carbonate]G of 95–96% using S of 10.6 and QT of 60 mL min−1. Characterization of the granules confirmed high purity calcium carbonate. Overall, the transformation of industrial CO2 emissions into a valuable solid product can be a significant move towards the mitigation of climate change from anthropogenic emissions.
KW - Carbonate influent
KW - Climate change
KW - Fluidized-bed reactor
KW - Granule characteristics
KW - Influx flow rate
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U2 - 10.1016/j.chemosphere.2020.126325
DO - 10.1016/j.chemosphere.2020.126325
M3 - Article
C2 - 32234625
AN - SCOPUS:85080115294
SN - 0045-6535
VL - 250
JO - Chemosphere
JF - Chemosphere
M1 - 126325
ER -