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Thermochemical Energy Storage Based on Carbonates

A special issue of Energies (ISSN 1996-1073). This special issue belongs to the section "D: Energy Storage and Application".

Deadline for manuscript submissions: closed (28 February 2022) | Viewed by 12697
Please submit your paper and select the Journal "Energies" and the Special Issue "Thermochemical Energy Storage Based on Carbonates" via: https://susy.mdpi.com/user/manuscripts/upload?journal=energies. Please contact the journal editor Adele Min ([email protected]) before submitting.

Special Issue Editor


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Guest Editor
Departamento de Ingeniería, Universidad Loyola Andalucía, 41704 Dos Hermanas, Sevilla, Spain
Interests: thermochemical energy storage; renewable energy; dispatchability; CO2 capture; concentrating solar power; photovoltaics; district heating systems; thermal energy storage; CCU
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Special Issue Information

Dear Colleagues,

Efficient, cost-effective, and scalable energy storage systems stand as one of the main technological challenges for the massive deployment of renewable energies. Thermochemical energy storage (TCES) is an attractive alternative to molten salt systems. TCES integrated into solar plants consist of using solar energy to produce an endothermic reaction and store the products. Under demand, the products are brought together, and the opposite exothermic reaction takes place to release the stored energy. Among TCES, carbonate-based systems are one of the most promising alternatives due to their high-turning temperature, high energy density, and, usually, low price of the raw materials. However, TCES is developed only at a laboratory scale, and some drawbacks, such as sorbent deactivation or agglomeration, need to be improved for the scaling up of the technology. Today, most studies are focused on the CaCO3/CaO system, although there are other potential options from PbCO3, SrCO3, BaCO3, and MgCO3.

This Special Issue covers all research concerning TCES based on carbonates. Topics of interest for publication include, but are not limited to, the following:

  • TCES modeling
  • Materials properties
  • Synthetic materials testing to improve the carbonate looping behavior
  • Reactors design for TCES
  • Power cycles integration on carbonate-based systems
  • Economic aspects
  • Scaling-up analysis
  • Critical reviews of TCES technology

Dr. Carlos Ortíz
Guest Editor

Manuscript Submission Information

Manuscripts should be submitted online at www.mdpi.com by registering and logging in to this website. Once you are registered, click here to go to the submission form. Manuscripts can be submitted until the deadline. All submissions that pass pre-check are peer-reviewed. Accepted papers will be published continuously in the journal (as soon as accepted) and will be listed together on the special issue website. Research articles, review articles as well as short communications are invited. For planned papers, a title and short abstract (about 100 words) can be sent to the Editorial Office for announcement on this website.

Submitted manuscripts should not have been published previously, nor be under consideration for publication elsewhere (except conference proceedings papers). All manuscripts are thoroughly refereed through a single-blind peer-review process. A guide for authors and other relevant information for submission of manuscripts is available on the Instructions for Authors page. Energies is an international peer-reviewed open access semimonthly journal published by MDPI.

Please visit the Instructions for Authors page before submitting a manuscript. The Article Processing Charge (APC) for publication in this open access journal is 2600 CHF (Swiss Francs). Submitted papers should be well formatted and use good English. Authors may use MDPI's English editing service prior to publication or during author revisions.

Keywords

  • Thermochemical energy storage
  • CaCO3
  • calcium-looping
  • dispatchability
  • energy density
  • high-temperature power cycles
  • TES

Published Papers (4 papers)

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Editorial

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3 pages, 373 KiB  
Editorial
Thermochemical Energy Storage Based on Carbonates: A Brief Overview
by Carlos Ortiz
Energies 2021, 14(14), 4336; https://0-doi-org.brum.beds.ac.uk/10.3390/en14144336 - 19 Jul 2021
Cited by 5 | Viewed by 1672
Abstract
Energy storage is becoming one of the main challenges facing the massive integration of Variable Renewable Energy (VRE) in the coming years [...] Full article
(This article belongs to the Special Issue Thermochemical Energy Storage Based on Carbonates)
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Research

Jump to: Editorial

20 pages, 2499 KiB  
Article
FMEA and Risks Assessment for Thermochemical Energy Storage Systems Based on Carbonates
by Andrés Carro, Ricardo Chacartegui, Carlos Tejada, Georgios Gravanis, Muhammad Eusha, Voutetakis Spyridon, Papadopoulou Simira and Carlos Ortiz
Energies 2021, 14(19), 6013; https://0-doi-org.brum.beds.ac.uk/10.3390/en14196013 - 22 Sep 2021
Cited by 3 | Viewed by 2653
Abstract
Thermochemical energy storage systems from carbonates, mainly those based on calcium carbonate, have been gaining momentum in the last few years. However, despite the considerable interest in the process, the Technology Readiness Level (TRL) is still low. Therefore, facing the progressive development of [...] Read more.
Thermochemical energy storage systems from carbonates, mainly those based on calcium carbonate, have been gaining momentum in the last few years. However, despite the considerable interest in the process, the Technology Readiness Level (TRL) is still low. Therefore, facing the progressive development of the technology at different scales is essential to carry out a comprehensive risk assessment and a Failure Mode Effect and Analysis (FMEA) process to guarantee the safety and operation of the technology systems. In this study, the methodology was applied to a first-of-its-kind prototype, and it is a valuable tool for assessing safe design and operation and potential scaling up. The present work describes the methodology for carrying out these analyses to construct a kW-scale prototype of an energy storage system based on calcium carbonate. The main potential risks occur during the testing and operation stages (>50% of identified risks), being derived mainly from potential overheating in the reactors, failures in the control of the solar shape at the receiver, and potential failures of the control system. Through the assessment of Risk Priority Numbers (RPNs), it was identified that the issues requiring more attention are related to hot fluid path to avoid loss of heat transfer and potential damages (personal and on the facilities), mainly due to their probability to occur (>8 on a scale of 10). The results derived from the FMEA analysis show the need for specific control measures in reactors, especially in the calciner, with high operation temperatures (1000 °C) and potential effects of overheating and corrosion. Full article
(This article belongs to the Special Issue Thermochemical Energy Storage Based on Carbonates)
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17 pages, 3512 KiB  
Article
Techno-Economic Assessment of Calcium Looping for Thermochemical Energy Storage with CO2 Capture
by Guillermo Martinez Castilla, Diana Carolina Guío-Pérez, Stavros Papadokonstantakis, David Pallarès and Filip Johnsson
Energies 2021, 14(11), 3211; https://0-doi-org.brum.beds.ac.uk/10.3390/en14113211 - 31 May 2021
Cited by 13 | Viewed by 3814
Abstract
The cyclic carbonation-calcination of CaCO3 in fluidized bed reactors not only offers a possibility for CO2 capture but can at the same time be implemented for thermochemical energy storage (TCES), a feature which will play an important role in a future [...] Read more.
The cyclic carbonation-calcination of CaCO3 in fluidized bed reactors not only offers a possibility for CO2 capture but can at the same time be implemented for thermochemical energy storage (TCES), a feature which will play an important role in a future that has an increasing share of non-dispatchable variable electricity generation (e.g., from wind and solar power). This paper provides a techno-economic assessment of an industrial-scale calcium looping (CaL) process with simultaneous TCES and CO2 capture. The process is assumed to make profit by selling dispatchable electricity and by providing CO2 capture services to a certain nearby emitter (i.e., transport and storage of CO2 are not accounted). Thus, the process is connected to two other facilities located nearby: a renewable non-dispatchable energy source that charges the storage and a plant from which the CO2 in its flue gas flow is captured while discharging the storage and producing dispatchable electricity. The process, which offers the possibility of long-term storage at ambient temperature without any significant energy loss, is herein sized for a given daily energy input under certain boundary conditions, which mandate that the charging section runs steadily for one 12-h period per day and that the discharging section can provide a steady output during 24 h per day. Intercoupled mass and energy balances of the process are computed for the different process elements, followed by the sizing of the main process equipment, after which the economics of the process are computed through cost functions widely used and validated in literature. The economic viability of the process is assessed through the breakeven electricity price (BESP), payback period (PBP), and as cost per ton of CO2 captured. The cost of the renewable energy is excluded from the study, although its potential impact on the process costs if included in the system is assessed. The sensitivities of the computed costs to the main process and economic parameters are also assessed. The results show that for the most realistic economic projections, the BESP ranges from 141 to −20 $/MWh for different plant sizes and a lifetime of 20 years. When the same process is assessed as a carbon capture facility, it yields a cost that ranges from 45 to −27 $/tCO2-captured. The cost of investment in the fluidized bed reactors accounts for most of the computed capital expenses, while an increase in the degree of conversion in the carbonator is identified as a technical goal of major importance for reducing the global cost. Full article
(This article belongs to the Special Issue Thermochemical Energy Storage Based on Carbonates)
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23 pages, 4898 KiB  
Article
An Experimental Study of the Decomposition and Carbonation of Magnesium Carbonate for Medium Temperature Thermochemical Energy Storage
by Daniel Mahon, Gianfranco Claudio and Philip Eames
Energies 2021, 14(5), 1316; https://0-doi-org.brum.beds.ac.uk/10.3390/en14051316 - 28 Feb 2021
Cited by 14 | Viewed by 3607
Abstract
To improve the energy efficiency of an industrial process thermochemical energy storage (TCES) can be used to store excess or typically wasted thermal energy for utilisation later. Magnesium carbonate (MgCO3) has a turning temperature of 396 °C, a theoretical potential to [...] Read more.
To improve the energy efficiency of an industrial process thermochemical energy storage (TCES) can be used to store excess or typically wasted thermal energy for utilisation later. Magnesium carbonate (MgCO3) has a turning temperature of 396 °C, a theoretical potential to store 1387 J/g and is low cost (~GBP 400/1000 kg). Research studies that assess MgCO3 for use as a medium temperature TCES material are lacking, and, given its theoretical potential, research to address this is required. Decomposition (charging) tests and carbonation (discharging) tests at a range of different temperatures and pressures, with selected different gases used during the decomposition tests, were conducted to gain a better understanding of the real potential of MgCO3 for medium temperature TCES. The thermal decomposition (charging) of MgCO3 has been investigated using thermal analysis techniques including simultaneous thermogravimetric analysis and differential scanning calorimetry (TGA/DSC), TGA with attached residual gas analyser (RGA) and diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) (up to 650 °C). TGA, DSC and RGA data have been used to quantify the thermal decomposition enthalpy from each MgCO3.xH2O thermal decomposition step and separate the enthalpy from CO2 decomposition and H2O decomposition. Thermal analysis experiments were conducted at different temperatures and pressures (up to 40 bar) in a CO2 atmosphere to investigate the carbonation (discharging) and reversibility of the decarbonation–carbonation reactions for MgCO3. Experimental results have shown that MgCO3.xH2O has a three-step thermal decomposition, with a total decomposition enthalpy of ~1050 J/g under a nitrogen atmosphere. After normalisation the decomposition enthalpy due to CO2 loss equates to 1030–1054 J/g. A CO2 atmosphere is shown to change the thermal decomposition (charging) of MgCO3.xH2O, requiring a higher final temperature of ~630 °C to complete the decarbonation. The charging input power of MgCO3.xH2O was shown to vary from 4 to 8136 W/kg with different isothermal temperatures. The carbonation (discharging) of MgO was found to be problematic at pressures up to 40 bar in a pure CO2 atmosphere. The experimental results presented show MgCO3 has some characteristics that make it a candidate for thermochemical energy storage (high energy storage potential) and other characteristics that are problematic for its use (slow discharge) under the experimental test conditions. This study provides a comprehensive foundation for future research assessing the feasibility of using MgCO3 as a medium temperature TCES material. Future research to determine conditions that improve the carbonation (discharging) process of MgO is required. Full article
(This article belongs to the Special Issue Thermochemical Energy Storage Based on Carbonates)
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