Abstract
The solid-state kinetics of Co-Ni/Al2O3 oxygen carrier is studied using non-isothermal reaction data and a non-linear regression analysis. XRD analysis of the fresh samples shows that NiO is the dominant reducible phase of the oxygen carrier. Pulse chemisorption suggests a negligible nuclei growth over the repeated reduction/oxidation cycles. Mercury porosimetry confirms that the pore size of the carrier particle is slightly increased following reduction. A nucleation and nuclei growth model and an unreacted shrinking-core model are developed based on the oxygen carrier texture change during reduction/oxidation, as observed by pulse chemisorption and mercury porosimetry. Model parameters are calculated using H2-TPR and O2-TPO data. It is found that the random nucleation model describes solid phase changes adequately. The determined apparent activation energies are 45 and 44 kJ/mol for the reduction and oxidation, respectively. The established kinetic model is successfully evaluated for the reduction cycle using a CREC mini-fluidized Riser Simulator reactor operating under expected conditions of large industrial scale fluidized CLC units.
| Original language | English |
|---|---|
| Pages (from-to) | 98-106 |
| Number of pages | 9 |
| Journal | Chemical Engineering Science |
| Volume | 65 |
| Issue number | 1 |
| DOIs | |
| State | Published - 2010 |
| Externally published | Yes |
Bibliographical note
Funding Information:M.M.H. wishes to acknowledge the Natural Sciences and Engineering Research Council of Canada (NSERC) for Canada Graduate Scholarship for Doctoral study (CGS-D) and The University of Western Ontario for President's Scholarship for Graduate Study (PSGS). The authors also like to thank NSERC for their financial support to this project.
Keywords
- CLC
- CO capture
- Gas-solid reaction kinetics
- Nucleation and nuclei growth model
- Shrinking-core model
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
- Industrial and Manufacturing Engineering