4.7 Article

Characterization and kinetics of reduction of CaSO4 with carbon monoxide for chemical-looping combustion

Journal

COMBUSTION AND FLAME
Volume 158, Issue 12, Pages 2524-2539

Publisher

ELSEVIER SCIENCE INC
DOI: 10.1016/j.combustflame.2011.05.011

Keywords

CO2 capture; Chemical-looping combustion; CaSO4-CaS-CaO cycle; Kinetics; Thermodynamics

Funding

  1. National Natural Science Foundation of China (NSFC) [51061130535, 50606006]
  2. National High Technology Research and Development Program of China (863 program) [2009AA05Z312]
  3. National Basic Research Program of China (973 Program) [2010CB732206]

Ask authors/readers for more resources

Chemical-looping combustion (CLC) of fuels via the cyclic reduction and oxidation of an oxygen carrier is a novel process for CO2 capture. CaSO4 has emerged as an alternative material with much lower cost and higher oxygen storage capacity compared to metal oxide based oxygen carrier. In principle, CaSO4 is reduced by CO and H-2 (coal gasification products) generating CaS, CO2 and H2O, and then the solid product CaS is regenerated back to CaSO4 in air. Research on the reactions of CaSO4 and CaS is not only important for understanding the reaction mechanism and parameters for the new CLC technology but also of high interest in understanding the sulfur chemistry in fluidized bed combustion and gasification. This paper focuses on the reduction reaction of CaSO4 with CO to CaS and CO2 (CaSO4 + 4CO -> CaS + 4CO(2)) by thermodynamics, characterization and kinetics analysis. Phase diagram of CaSO4-CaO-CaS indicates the operation regime of reduction-oxidation cycle by delicate control of temperature and partial pressure of reaction gases. The kinetics of the reduction reaction of a low cost natural anhydrite as oxygen carrier was investigated in an isothermal differential bed reactor where a thin layer of CaSO4 particles were exposed to a plug flow of CO balanced by N-2. Prior to the kinetics modeling, extensive physical and chemical characterization analyses, such as X-ray diffraction (XRD), scanning electron microscopy with energy-dispersive X-ray spectroscopy (SEM-EDX), and N-2 adsorption-desorption were carried out to understand the reaction mechanism. External mass transfer and heat effects were minimized and the operation regime for intrinsic kinetics was determined. The experimental data was described with a gas-solid shrinking unreacted core model (SCM) with both chemical reaction control and product layer diffusion resistance considered. (C) 2011 The Combustion Institute. Published by Elsevier Inc. All rights reserved.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.7
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available