LAPSE:2026.0345
Published Article

LAPSE:2026.0345
Simulation of Fixed-Bed Reactor System for Combined Ca-Cu Chemical Looping with Integrated Combustion and CO2 Capture
July 6, 2026. Originally submitted on June 12, 2026
Abstract
As greenhouse gas emissions accelerate global warming, new capture and storage technologies are essential for reducing the industrial CO2 concentration in the atmosphere. This study addresses the urgent need for greenhouse gas capture technologies by developing a detailed dynamic mathematical model for Chemical Looping Process with Integrated Combustion and CO2 capture (CL-ICCC). In the CL-ICCC process configuration, CO2 capture is integrated into the chemical looping combustion system, resulting in a higher-purity, more efficient process. In this work Cu/CuO oxygen carrier material and CaO/CaCO3 sorbent materials were considered in a fixed bed reactor as solid phase to investigate Oxidation and Reduction/Calcination processes under different operating conditions. The simulation results were compared with experimental results from the literature. In case of the oxidation process, a sensitivity study was performed to investigate the behavior of the process for variation of different operating parameters under dynamic conditions: gas composition, initial gas temperature and solid phase mass composition. In the case of reduction/calcination, multiple fuel type and solid composition were investigated.
As greenhouse gas emissions accelerate global warming, new capture and storage technologies are essential for reducing the industrial CO2 concentration in the atmosphere. This study addresses the urgent need for greenhouse gas capture technologies by developing a detailed dynamic mathematical model for Chemical Looping Process with Integrated Combustion and CO2 capture (CL-ICCC). In the CL-ICCC process configuration, CO2 capture is integrated into the chemical looping combustion system, resulting in a higher-purity, more efficient process. In this work Cu/CuO oxygen carrier material and CaO/CaCO3 sorbent materials were considered in a fixed bed reactor as solid phase to investigate Oxidation and Reduction/Calcination processes under different operating conditions. The simulation results were compared with experimental results from the literature. In case of the oxidation process, a sensitivity study was performed to investigate the behavior of the process for variation of different operating parameters under dynamic conditions: gas composition, initial gas temperature and solid phase mass composition. In the case of reduction/calcination, multiple fuel type and solid composition were investigated.
Record ID
Keywords
Carbon Dioxide Capture, Chemical Looping, Fixed-Bed Reactor, Hydrogen generation, Sensitivity Study
Subject
Suggested Citation
Biró L, Mihály N, Cormoș A. Simulation of Fixed-Bed Reactor System for Combined Ca-Cu Chemical Looping with Integrated Combustion and CO2 Capture. Systems and Control Transactions 5:1127-1134 (2026) https://doi.org/10.69997/sct.185375
Author Affiliations
Biró L: Babeș - Bolyai University, Department of Chemical Engineering, Cluj-Napoca, Romania [ORCID]
Mihály N: Babeș - Bolyai University, Department of Chemical Engineering, Cluj-Napoca, Romania [ORCID]
Cormoș A: Babeș - Bolyai University, Department of Chemical Engineering, Cluj-Napoca, Romania [ORCID]
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Mihály N: Babeș - Bolyai University, Department of Chemical Engineering, Cluj-Napoca, Romania [ORCID]
Cormoș A: Babeș - Bolyai University, Department of Chemical Engineering, Cluj-Napoca, Romania [ORCID]
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Journal Name
Systems and Control Transactions
Volume
5
First Page
1127
Last Page
1134
Year
2026
Publication Date
2026-06-12
Version Comments
Minor corrections to Figure 1
Other Meta
PII: 1127-1134-263-SCT-5-2026, Publication Type: Journal Article
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LAPSE:2026.0345
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https://doi.org/10.69997/sct.185375
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References Cited
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