Reaction Kinetics in Chemical Looping Processes

A special issue of Fire (ISSN 2571-6255). This special issue belongs to the section "Mathematical Modelling and Numerical Simulation of Combustion and Fire".

Deadline for manuscript submissions: 30 June 2025 | Viewed by 1705

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Department of Energy and Environment, CSIC-Instituto de Carboquimica (ICB), Zaragoza, Spain
Interests: development of advanced and clean combustion processes in fluidized bed reactors to produce energy with CO2 capture; in recent years, I have had intense activity in the development of chemical looping technologies, mainly focused on the advance of oxygen carriers, reaction kinetics, modeling reactors, design and operation of pilot plants, as well as techno-economic assessment
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Special Issue Information

Dear Colleagues,

I am pleased to invite you to submit a manuscript to this Special Issue of Fire, titled “Reaction Kinetics in Chemical Looping Processes”.

Chemical looping processes are based on splitting a chemical process into two or more steps in a cyclic way. Typically, an active material is used as a carrier that connects the different stages of the chemical looping process. In the beginning, chemical looping was proposed as an advanced combustion process with the potential to increase energy efficiency in the thermochemical conversion of fuels using the principles of thermodynamics to reduce exergy loss. Thus, an oxygen carrier was used to split the combustion process into two stages. Thus, Chemical Looping Combustion (CLC) was characterized by obtaining a CO2 stream separated from the depleted air used for fuel combustion. Due to this, CLC was shown to be one of the most promising technologies for combustion with CO2 capture at low energy and economic costs. However, the development of chemical looping technology has been extended to diverse processes for multiple purposes. These processes may be based on the transference of one atom or compound for fuel oxidation, reducing a compound, gas separation, chemical synthesis, or circumvent thermochemical equilibrium limitations in chemical reactions.

This Special Issue aims to disseminate new and relevant research in a unique publication on the kinetics of reactions involved in different chemical looping processes, including, but not limited to, the following:

  • Combustion for energy production: An oxygen carrier transport oxygen from air to fuel for its combustion. Processes include Chemical Looping Combustion (CLC) and Chemical Looping with Oxygen Uncoupling (CLOU).
  • Syngas production: An oxygen carrier provides oxygen for the partial oxidation of a fuel to produce syngas. Chemical Looping Reforming (CLR) is focused on gaseous or liquid fuels, while solid fuels are used in Chemical Looping Gasification (CLG).
  • CO2 separation: A CO2 carrier is used to separate CO2 from a gaseous stream. Calcium carbonate has been extensively studied for this process in so-called Calcium Looping (CaL), but other CO2 carriers may be used, including lithium orthosilicates or sodium zirconates.
  • Hydrogen production: A water splitting reaction is integrated in the chemical loop to produce hydrogen by the partial oxidation of the oxygen carrier by H2 Several configurations have been proposed, which may be described as Chemical Looping with Water Splitting (CLWS) processes. A concentrated H2 stream is also the purpose of so-called sorption enhanced chemical looping reforming (SE-CLR) or gasification (SE-CLG) processes, where bi-functional oxygen and CO2 carriers are used.
  • CO2 use: In chemical looping with CO2 splitting (CLCO2S), CO is produced by the CO2 splitting reaction assisted by an oxygen carrier.
  • Ammonia production: Nitrogen carriers are used to produce ammonia more efficiently than the traditional Haber–Bosch process.
  • Circumvent limitations of thermodynamic equilibrium: Eliminating one product of the reaction, such as steam in sorption enhanced methanation (SEM) or selective hydrogen oxidation in oxidative de-hydrogenation reactions.
  • Gas purification: Including processes in which a chemical loop may be used for selective oxidation of one compound in a gas mixture, or the avoidance of harmful emissions, e.g., in ventilation air methane.
In this Special Issue, original research articles and reviews are welcome. Research areas may include (but are not limited to) the following:
  • Theoretical studies, such as those based on density functional theory (DFT) or focused on unrevealing reaction mechanisms and the experimental determination of reaction kinetics involving oxygen, CO2, water, or nitrogen carriers, such as:
  • Reduction and oxidation reactions of oxygen carriers for CLC, CLOU, CLR, and CLG.
  • Kinetics of catalytic reactions supported by oxygen carriers.
  • Carbonation/calcination reactions of CO2
  • Splitting reactions with an oxygen carrier and H2O or CO2.
  • Nitrogen reaction with nitrogen carriers or N-carrier reaction to form ammonia.
  • Kinetics involved in fuel conversion in chemical looping processes.

I look forward to receiving your contributions.

Dr. Alberto Abad Secades
Guest Editor

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Keywords

  • chemical looping
  • kinetics
  • oxygen carrier
  • CO2 carrier
  • nitrogen carrier
  • combustion
  • reforming
  • gasification
  • ammonia
  • CO2 capture

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Published Papers (2 papers)

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Research

16 pages, 5916 KiB  
Article
Numerical Investigation of Force Network Evolution in a Moving Bed Air Reactor
by Wei Dai, Yali Shao, Shangyi Yin, Tao Song and Ramesh K. Agarwal
Fire 2024, 7(11), 376; https://doi.org/10.3390/fire7110376 - 24 Oct 2024
Viewed by 455
Abstract
In spite of extensive research on macroscopic solid movements in the dense granular system of a moving bed air reactor, research on the evolution characteristics of the mesoscale inter-particle contact force network is still lacking. In this work, discrete element simulations are conducted [...] Read more.
In spite of extensive research on macroscopic solid movements in the dense granular system of a moving bed air reactor, research on the evolution characteristics of the mesoscale inter-particle contact force network is still lacking. In this work, discrete element simulations are conducted to investigate the force chain structure properties in a moving bed air reactor. The results show that during the particle discharging process, the force chain network exhibits great anisotropy, and force chain contacts account for only about 13–14% of all inter-particle contacts, while the strong particle–particle contacts account for about 37–41% of all the particle–particle interactions. The collimation coefficients of force chains are more stable at the early stages and then decrease sharply over time. Both particle–particle and particle–wall friction coefficients affect the number, strength, collimation coefficient, and direction of force chains but have little influence on the length distribution of force chains. An in-depth analysis of the evolution of the force network provides new insights for further understanding dense granular flow in a moving bed air reactor for chemical looping combustion. Full article
(This article belongs to the Special Issue Reaction Kinetics in Chemical Looping Processes)
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12 pages, 3599 KiB  
Article
Kinetics Investigation of Copper Ore Oxygen Carrier for Chemical Looping Combustion
by Xin Tian, Mingze Su and Haibo Zhao
Fire 2024, 7(7), 245; https://doi.org/10.3390/fire7070245 - 12 Jul 2024
Viewed by 821
Abstract
Chemical looping combustion (CLC) has been validated as one of the most promising technologies for fossil fuel combustion, which can produce high-purity CO2 streams ready for capture and sequestration in power production. The selection of an appropriate oxygen carrier is one of [...] Read more.
Chemical looping combustion (CLC) has been validated as one of the most promising technologies for fossil fuel combustion, which can produce high-purity CO2 streams ready for capture and sequestration in power production. The selection of an appropriate oxygen carrier is one of the most important issues for the CLC process, and the reduction kinetics investigation of the oxygen carrier with fuel gas can provide the basis for CLC reactor design and simulation optimization. In this study, copper ore was chosen as an oxygen carrier, and the oxygen release property of copper ore under a nitrogen environment at various temperatures (1073–1193 K) was first investigated in a thermogravimetric analyzer (TGA). Subsequently, the reduction kinetics of copper ore with CO and H2 were evaluated by the TGA at temperatures ranging from 773 K to 1073 K, using a continuous stream of 5, 10, 15, 20, 25, and 30 vol. % of CO or H2 balanced by CO2 or N2. It was found that the reaction rates of these reactions accelerated with the increase in temperature and fuel gas concentration in inlet gas. Both the oxygen release process of copper ore and the reduction process of copper ore with reducing gases can be described by the unreacted shrinking core model (USCM). The reaction mechanism function for the oxygen-releasing and reduction process of copper ore oxygen carrier was varied. The activation energy of the oxygen-releasing process, reduction process with CO, and reduction process with H2 were calculated as 99.35, 5.08, and 4.28 kJ/mol, respectively. The pre-exponential factor ranged from 1.96 × 10−1 to 1.84 × 103. The reaction order depended on the fuel gas, which was 1 and 0.86, respectively, for reaction with CO and H2. Full article
(This article belongs to the Special Issue Reaction Kinetics in Chemical Looping Processes)
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