Factors affecting the precipitation of pure calcium carbonate during the direct aqueous carbonation of flue gas desulfurization gypsum

The mineral carbonation of FGD (flue gas desulfurization) gypsum was carried out through CO2 sorption into ammonia solution containing FGD gypsum. High-purity calcium carbonate was precipitated from DCC (dissolved calcium carbonate) solution which was extracted during the induction period. The facto...

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Published inEnergy (Oxford) Vol. 65; pp. 527 - 532
Main Authors KYUNGSUN SONG, JANG, Young-Nam, WONBAEK KIM, MYUNG GYU LEE, DONGBOK SHIN, BANG, Jun-Hwan, CHI WAN JEON, SOO CHUN CHAE
Format Journal Article
LanguageEnglish
Published Kidlington Elsevier 01.02.2014
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Summary:The mineral carbonation of FGD (flue gas desulfurization) gypsum was carried out through CO2 sorption into ammonia solution containing FGD gypsum. High-purity calcium carbonate was precipitated from DCC (dissolved calcium carbonate) solution which was extracted during the induction period. The factors affecting the preparation of pure calcium carbonate were examined under the following conditions: CO2 flow rate (1-3 L/min), ammonia content (4-12%), and S/L (solid-to-liquid) ratio (5-300 g/L). X-Ray diffraction study revealed that the PCC (precipitated calcium carbonate) was round-shaped vaterite. The induction time for PCC decreased as the CO2 flow rate increased. The maximum formation efficiency for pure PCC was seen to increase linearly with the ammonia content. The formation efficiency for pure PCC was the highest (90%) for S/L ratio of 5 g/L but it decreased as S/L ratio increased. On the other hand, S/L ratio didn't affect the maximum solubility limit of DCC. It is believed that the pure PCC would add an economic value to the FGD gypsum carbonation for industrial CO2 sequestration.
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ISSN:0360-5442
DOI:10.1016/j.energy.2013.11.008