Oxy-Fuel combustion in an entrained flow reactor for regeneration of spent Calcium Looping sorbents

• Demonstration of entrained flow calcination in oxy-fuel atmosphere for CO 2 capture. • Usage of spent sorbent from novel Calcium Looping process based on Ca(OH) 2. • Comparing experimental results to kinetic model shows reasonable results. • Complete conversion to CaO under oxy-fuel conditions possible within 10 s. Calcium Looping (CaL) is one of the most promising technologies for large-scale CO 2 capture of flue gases from power plants and industrial processes. A Ca-based sorbent, mostly CaO derived from limestone, is used to capture CO 2 in the first step, while being regenerated in the second step. The aim of this study was to investigate the regeneration step of a novel CaL concept, which uses Ca(OH) 2 as CO 2 capture sorbent for backup power plants (“BackCap” concept). The spent sorbent after CO 2 capture was calcined in an entrained flow reactor, using oxy-fuel conditions. In particular, the calcination degrees of the sorbent that were reached during a few seconds residence time in the reactor, were of main interest in this study. Therefore, experiments including parameter variations were carried out in a drop-tube and an entrained flow reactor to calcine the carbonated Ca(OH) 2 particles. Calcination degrees of almost 0.6 were reached within the test facility used, while calcining in short residence times (i.e. <5 s) under oxy-fuel conditions. The experimental results obtained were implemented into a calcination model, indicating that full calcination of particles under oxy-fuel conditions is possible within reasonable residence time (i.e. 10 s).

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Publication Details

Journal
Fuel
Published
2024-11-23
DOI
https://doi.org/10.1016/j.fuel.2024.133784
Citations
1
Primary Topic
Chemical Looping and Thermochemical Processes
Type
article
Field-Weighted Citation Impact
0.18

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article

Oxy-Fuel combustion in an entrained flow reactor for regeneration of spent Calcium Looping sorbents

Günter Scheffknecht, B. Arias, Nico Mader, Jörg Maier
1 citations
Fuel
Chemical Looping and Thermochemical Processes
0.18
article

Oxy-Fuel combustion in an entrained flow reactor for regeneration of spent Calcium Looping sorbents

Günter Scheffknecht, B. Arias, Nico Mader, Jörg Maier
article en
1 citations

Abstract

• Demonstration of entrained flow calcination in oxy-fuel atmosphere for CO 2 capture. • Usage of spent sorbent from novel Calcium Looping process based on Ca(OH) 2. • Comparing experimental results to kinetic model shows reasonable results. • Complete conversion to CaO under oxy-fuel conditions possible within 10 s. Calcium Looping (CaL) is one of the most promising technologies for large-scale CO 2 capture of flue gases from power plants and industrial processes. A Ca-based sorbent, mostly CaO derived from limestone, is used to capture CO 2 in the first step, while being regenerated in the second step. The aim of this study was to investigate the regeneration step of a novel CaL concept, which uses Ca(OH) 2 as CO 2 capture sorbent for backup power plants (“BackCap” concept). The spent sorbent after CO 2 capture was calcined in an entrained flow reactor, using oxy-fuel conditions. In particular, the calcination degrees of the sorbent that were reached during a few seconds residence time in the reactor, were of main interest in this study. Therefore, experiments including parameter variations were carried out in a drop-tube and an entrained flow reactor to calcine the carbonated Ca(OH) 2 particles. Calcination degrees of almost 0.6 were reached within the test facility used, while calcining in short residence times (i.e. <5 s) under oxy-fuel conditions. The experimental results obtained were implemented into a calcination model, indicating that full calcination of particles under oxy-fuel conditions is possible within reasonable residence time (i.e. 10 s).

FuelVol. 381
University of Stuttgart (DE), Instituto Nacional del Carbón (ES)
European Commission, Research Fund for Coal and Steel
Affordable and clean energy
Openalex Percentile: Top 50%
Chemical Looping and Thermochemical Processes
0.18
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