Literature DB >> 23734593

Kinetics and mechanism of direct reaction between CO2 and Ca(OH)2 in micro fluidized bed.

Jian Yu1, Xi Zeng, Guangyi Zhang, Juwei Zhang, Yin Wang, Guangwen Xu.   

Abstract

Even at present it is still difficult to characterize the reaction between CO2 and Ca(OH)2 at high temperature and atmospheric pressure using traditional instruments such as thermogravimetric analyzer and differential scanning calorimeter. This study was devoted to characterizing such a reaction in a newly developed micro fluidized bed reaction analyzer (MFBRA) under isothermal conditions in the temperature range of 773-1023 K. The results indicated that the MFBRA has not only a good adaptability for characterizing the above-mentioned reaction but enables as well a new insight into the mechanism of the reaction. An obvious time delay was identified for the release of the formed steam (H2O) in comparison with the onset of its CO2 absorption, which might be attributed to the formation of an unstable intermediate product Ca(HCO3)2 in the reaction process between CO2 and Ca(OH)2. The activation energy for forming Ca(HCO3)2 was found to be about 40 kJ/mol, which is much lower than that of the reaction between CO2 and CaO.

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Year:  2013        PMID: 23734593     DOI: 10.1021/es4001196

Source DB:  PubMed          Journal:  Environ Sci Technol        ISSN: 0013-936X            Impact factor:   9.028


  2 in total

1.  Carbonation Kinetics of Ca(OH)2 Under Conditions of Entrained Reactors to Capture CO2.

Authors:  B Arias; Y A Criado; B Pañeda; J C Abanades
Journal:  Ind Eng Chem Res       Date:  2022-02-24       Impact factor: 3.720

2.  Analysis of Operation Conditions of Ca(OH)2 Entrained Carbonator Reactors for CO2 Capture in Backup Power Plants.

Authors:  Yolanda Alvarez Criado; Borja Arias
Journal:  ACS Omega       Date:  2022-08-04
  2 in total

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