Federica Raganati
Federica Raganati has a total of 39 co-authors. Here are the top co-authors by number of shared publications:
- Paola Ammendola
Istituto di Scienze e Tecnologie per l’Energia e la Mobilità Sostenibili (STEMS), Consiglio Nazionale delle Ricerche (CNR), Piazzale Tecchio 80, 80125 Naples, Italy
35 shared publications - Riccardo Chirone
Istituto di Ricerche sulla Combustione, Consiglio Nazionale delle Ricerche, Piazzale Vincenzo Tecchio 80, 80125 Napoli, Italy
11 shared publications Riccardo Chirone
10 shared publicationsR. Chirone
Institute for Research on Combustion (IRC), CNR, Naples, Italy
5 shared publications- Francesco Miccio
National Research Council of Italy CNR-ISSMC, via Granarolo 64, 48018 Faenza, Italy
4 shared publications - Michela Alfè
Consiglio Nazionale delle Ricerche (CNR)─Institute of Sciences and Technologies for Sustainable Energy and Mobility (STEMS)
4 shared publications
Latest Publications
- Open Access
- 6 July 2026
- Published by American Chemical Society (ACS) in Energy & Fuels
Adsorption Isotherm Modeling for Post-Combustion CO 2 Capture: A Critical Review and Engineering Perspective
- 6 July 2026
- Published by American Chemical Society (ACS) in Energy & Fuels
Open AccessAdsorption Isotherm Modeling for Post-Combustion CO 2 Capture: A Critical Review and Engineering Perspective
- Open Access
- 25 October 2025
- Published by Elsevier in Biomass and Bioenergy
- Vol. 205
Biogas production through combined thermochemical and biochemical processing of grape pomace
- 25 October 2025
- Published by Elsevier in Biomass and Bioenergy
- Vol. 205
Open AccessBiogas production through combined thermochemical and biochemical processing of grape pomace
- Top Cited PapersOpen Access
- 25 January 2025
- Published by Elsevier in Chemical Engineering Journal
- Vol. 506
CALF-20 obtained by mechanochemical synthesis for temperature swing adsorption CO2 Capture: A thermodynamic and kinetic study
- 25 January 2025
- Published by Elsevier in Chemical Engineering Journal
- Vol. 506
Top Cited PapersOpen AccessCALF-20 obtained by mechanochemical synthesis for temperature swing adsorption CO2 Capture: A thermodynamic and kinetic study
- Top Cited Papers
- 15 July 2024
- Published by American Chemical Society (ACS) in Energy & Fuels
- Vol. 38 (15) , 13858-13905
CO2 Post-combustion Capture: A Critical Review of Current Technologies and Future Directions
- 15 July 2024
- Published by American Chemical Society (ACS) in Energy & Fuels
- Vol. 38 (15) , 13858-13905
Top Cited PapersCO2 Post-combustion Capture: A Critical Review of Current Technologies and Future Directions
- Top Cited Papers
- 13 January 2023
- Published by American Chemical Society (ACS) in Energy & Fuels
- Vol. 37 (3) , 1777-1808
Review of Carbonate-Based Systems for Thermochemical Energy Storage for Concentrating Solar Power Applications: State-of-the-Art and Outlook
- 13 January 2023
- Published by American Chemical Society (ACS) in Energy & Fuels
- Vol. 37 (3) , 1777-1808
Top Cited PapersReview of Carbonate-Based Systems for Thermochemical Energy Storage for Concentrating Solar Power Applications: State-of-the-Art and Outlook
- Open Access
- 10 January 2022
- Published by Hosokawa Powder Technology Foundation in KONA Powder and Particle Journal
- Vol. 39 (39) , 240-250
Carbonation Kinetics of Fine CaO Particles in a Sound-Assisted Fluidized Bed for Thermochemical Energy Storage
The calcium-looping process, relying on the reversible calcination/carbonation of CaCO3, is one of the most promising solution to perform thermochemical energy storage (TCES) for concentrating solar power (CSP) plants. Indeed, CaO precursors such as limestone can rely on the high energy density, low cost, large availability and nontoxicity. In this work, the study of the sound-assisted carbonation of fine CaO particles (< 50 μm) for TCES-CSP has been furthered. In particular, a kinetic study has been performed to analyse the effect of the particular carbonation conditions to be used in TCES-CSP applications, i.e. involving carbonation under high CO2 partial pressure and at high temperature. All the experimental tests have been performed in a lab-scale sound-assisted fluidized bed reactor applying high intensity acoustic field with proper frequency (150 dB–120 Hz). The carbonation kinetics has been analysed by applying a simple kinetic model, able to properly describe the fast (under kinetic control) and slow (under diffusion control) stage of the of the reaction. In particular, the reaction rate, the intrinsic carbonation kinetic constant and the characteristic product layer thickness have been evaluated, also highlighting their dependence on the temperature between 800 and 845 °C; a value of 49 kJ mol–1 has been obtained for the activation energy. Finally, a good agreement between the conversion-time profiles, evaluated from the applied kinetic models, and the experimental data has been obtained.
- 10 January 2022
- Published by Hosokawa Powder Technology Foundation in KONA Powder and Particle Journal
- Vol. 39 (39) , 240-250
Open AccessCarbonation Kinetics of Fine CaO Particles in a Sound-Assisted Fluidized Bed for Thermochemical Energy Storage
The calcium-looping process, relying on the reversible calcination/carbonation of CaCO3, is one of the most promising solution to perform thermochemical energy storage (TCES) for concentrating solar power (CSP) plants. Indeed, CaO precursors such as limestone can rely on the high energy density, low cost, large availability and nontoxicity. In this work, the study of the sound-assisted carbonation of fine CaO particles (< 50 μm) for TCES-CSP has been furthered. In particular, a kinetic study has been performed to analyse the effect of the particular carbonation conditions to be used in TCES-CSP applications, i.e. involving carbonation under high CO2 partial pressure and at high temperature. All the experimental tests have been performed in a lab-scale sound-assisted fluidized bed reactor applying high intensity acoustic field with proper frequency (150 dB–120 Hz). The carbonation kinetics has been analysed by applying a simple kinetic model, able to properly describe the fast (under kinetic control) and slow (under diffusion control) stage of the of the reaction. In particular, the reaction rate, the intrinsic carbonation kinetic constant and the characteristic product layer thickness have been evaluated, also highlighting their dependence on the temperature between 800 and 845 °C; a value of 49 kJ mol–1 has been obtained for the activation energy. Finally, a good agreement between the conversion-time profiles, evaluated from the applied kinetic models, and the experimental data has been obtained.
- Open Access
Fluidized Bed Combustion and Gasification of Fossil and Renewable Slurry Fuels
This article provides a comprehensive review of the state of the art and more recent developments of the thermochemical treatments of slurry fuels in fluidized beds (FB). The review focuses on FB combustion and gasification of slurry fuels based on coal, biomass, sludge, and wastes from industry, agriculture, and the civil sector. The investigations at research and industrial levels over the last decades are presented and discussed, highlighting the adopted technological solutions, the results in terms of feasibility and efficiency, and the perspectives of future development. The different behavior between bubbling and circulating beds was addressed, in particular the optimal choice depending on the process (combustion/gasification/pyrolysis) and fuel properties (e.g., water content). Fundamental studies on interactions between the slurry fuels and the hot bed materials are also reviewed. The cumulative trend of reviewed investigations over the last decades depicts the abandonment of coal-based mixtures used in large plants, and the growing interest in the use of biomass-based slurries for small size application. In this respect, the shift from coal to biomass opens new challenges because of the different properties of biomass (density, fibrous structure, spontaneous degradation, hydrophilic behavior, etc.). Biomass-based slurries circumvent problems posed by using solid dry biomass, particularly in handling, storing, and feeding. Although slurry fuels represent a narrow sector, the results of the research investigations and the experience gained with coal can be exploited to contribute to the achievement of a circular approach based on renewable resources in the near future.
Open AccessFluidized Bed Combustion and Gasification of Fossil and Renewable Slurry Fuels
This article provides a comprehensive review of the state of the art and more recent developments of the thermochemical treatments of slurry fuels in fluidized beds (FB). The review focuses on FB combustion and gasification of slurry fuels based on coal, biomass, sludge, and wastes from industry, agriculture, and the civil sector. The investigations at research and industrial levels over the last decades are presented and discussed, highlighting the adopted technological solutions, the results in terms of feasibility and efficiency, and the perspectives of future development. The different behavior between bubbling and circulating beds was addressed, in particular the optimal choice depending on the process (combustion/gasification/pyrolysis) and fuel properties (e.g., water content). Fundamental studies on interactions between the slurry fuels and the hot bed materials are also reviewed. The cumulative trend of reviewed investigations over the last decades depicts the abandonment of coal-based mixtures used in large plants, and the growing interest in the use of biomass-based slurries for small size application. In this respect, the shift from coal to biomass opens new challenges because of the different properties of biomass (density, fibrous structure, spontaneous degradation, hydrophilic behavior, etc.). Biomass-based slurries circumvent problems posed by using solid dry biomass, particularly in handling, storing, and feeding. Although slurry fuels represent a narrow sector, the results of the research investigations and the experience gained with coal can be exploited to contribute to the achievement of a circular approach based on renewable resources in the near future.
- Open Access
Sound-Assisted Fluidization for Temperature Swing Adsorption and Calcium Looping: A Review
Fine/ultra-fine cohesive powders find application in different industrial and chemical sectors. For example, they are considered in the framework of the Carbon Capture and Storage (CCS), for the reduction of the carbon dioxide emissions to the atmosphere, and in the framework of the thermochemical energy storage (TCES) in concentrated solar power (CSP) plants. Therefore, developing of technologies able to handle/process big amounts of these materials is of great importance. In this context, the sound-assisted fluidized bed reactor (SAFB) designed and set-up in Naples represents a useful device to study the behavior of cohesive powders also in the framework of low and high temperature chemical processes, such as CO2 adsorption and Ca-looping. The present manuscript reviews the main results obtained so far using the SAFB. More specifically, the role played by the acoustic perturbation and its effect on the fluid dynamics of the system and on the performances/outcomes of the specific chemical processes are pointed out.
Open AccessSound-Assisted Fluidization for Temperature Swing Adsorption and Calcium Looping: A Review
Fine/ultra-fine cohesive powders find application in different industrial and chemical sectors. For example, they are considered in the framework of the Carbon Capture and Storage (CCS), for the reduction of the carbon dioxide emissions to the atmosphere, and in the framework of the thermochemical energy storage (TCES) in concentrated solar power (CSP) plants. Therefore, developing of technologies able to handle/process big amounts of these materials is of great importance. In this context, the sound-assisted fluidized bed reactor (SAFB) designed and set-up in Naples represents a useful device to study the behavior of cohesive powders also in the framework of low and high temperature chemical processes, such as CO2 adsorption and Ca-looping. The present manuscript reviews the main results obtained so far using the SAFB. More specifically, the role played by the acoustic perturbation and its effect on the fluid dynamics of the system and on the performances/outcomes of the specific chemical processes are pointed out.
- 1 August 2020
- Published by Elsevier in Powder Technology
- Vol. 373, 446-458
Fixed bed adsorption as affected by thermodynamics and kinetics: Yellow tuff for CO2 capture
- 1 August 2020
- Published by Elsevier in Powder Technology
- Vol. 373, 446-458
Fixed bed adsorption as affected by thermodynamics and kinetics: Yellow tuff for CO2 capture