Integrated Mg-Cl hydrogen production process and CaO/CaCO3-CaCl2 thermochemical energy storage phase change system using solar tower system

[Display omitted] •A hybrid phase change CaO/CaCO3-CaCl2 thermochemical energy storage system is investigated.•A Mg-Cl hydrogen production process is developed using solar thermal energy.•Total exergy efficiencies of the energy storage system and Mg-Cl cycle are 62.2% and 84.3%.•Annual system effici...

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Veröffentlicht in:Energy conversion and management 2021-10, Vol.245, p.114555, Article 114555
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Pourmoghadam, Peyman
description [Display omitted] •A hybrid phase change CaO/CaCO3-CaCl2 thermochemical energy storage system is investigated.•A Mg-Cl hydrogen production process is developed using solar thermal energy.•Total exergy efficiencies of the energy storage system and Mg-Cl cycle are 62.2% and 84.3%.•Annual system efficiency, exergy efficiency and solar fraction are 63.74%, 54.76, and 83.59%, respectively. Hydrogen has been considered as a clean and sustainable fuel to meet heat requirements. The Mg-Cl hydrogen production cycle has been introduced as a promising thermochemical low-temperature cycle. In this paper, a solar system is integrated with a Mg-Cl cycle and a phase change CaO/CaCO3-CaCl2 thermochemical energy storage system (TCES). The heat generated by the solar tower is stored by the TCES in the charge mode. In the cases of low solar radiation, the TCES cycle stands in discharge mode and, if necessary, an auxiliary heat exchanger is utilized to provide the heat for the Mg-Cl cycle. The solar system is modeled by EES software and the other two cycles are simulated by Aspen Plus. Sensitivity and exergy analyses were performed for the system and reported along with the annual results of the whole system. The amount of 11.01 MW heat is stored in the charge mode and 9.536 MW is released in the discharge mode and 35.6 mol/s of hydrogen is acquired by the Mg-Cl cycle. The total exergy efficiencies of the TCES system and Mg-Cl cycle are 62.2% and 84.3%. The Mg-Cl cycle efficiency is enhanced due to the heat recovery of the internal streams and the TCES cycle efficiency is elevated due to the phase change process. The most exergy destroyer components of the TCES and Mg-Cl units belong to Carbonation and Electrolysis1 reactors with the value of 663.7 kW and 3747.4 kW, respectively. According to annual analysis, the most exergy destructions are related to the Electrolysis1 reactor, followed by solar system, which comprise 29.73% and 23.4% of total annual exergy destruction, respectively. Moreover, the annual system efficiency, exergy efficiency and solar fraction are 63.74%, 54.76, and 83.59%, respectively.
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Hydrogen has been considered as a clean and sustainable fuel to meet heat requirements. The Mg-Cl hydrogen production cycle has been introduced as a promising thermochemical low-temperature cycle. In this paper, a solar system is integrated with a Mg-Cl cycle and a phase change CaO/CaCO3-CaCl2 thermochemical energy storage system (TCES). The heat generated by the solar tower is stored by the TCES in the charge mode. In the cases of low solar radiation, the TCES cycle stands in discharge mode and, if necessary, an auxiliary heat exchanger is utilized to provide the heat for the Mg-Cl cycle. The solar system is modeled by EES software and the other two cycles are simulated by Aspen Plus. Sensitivity and exergy analyses were performed for the system and reported along with the annual results of the whole system. The amount of 11.01 MW heat is stored in the charge mode and 9.536 MW is released in the discharge mode and 35.6 mol/s of hydrogen is acquired by the Mg-Cl cycle. The total exergy efficiencies of the TCES system and Mg-Cl cycle are 62.2% and 84.3%. The Mg-Cl cycle efficiency is enhanced due to the heat recovery of the internal streams and the TCES cycle efficiency is elevated due to the phase change process. The most exergy destroyer components of the TCES and Mg-Cl units belong to Carbonation and Electrolysis1 reactors with the value of 663.7 kW and 3747.4 kW, respectively. According to annual analysis, the most exergy destructions are related to the Electrolysis1 reactor, followed by solar system, which comprise 29.73% and 23.4% of total annual exergy destruction, respectively. 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Hydrogen has been considered as a clean and sustainable fuel to meet heat requirements. The Mg-Cl hydrogen production cycle has been introduced as a promising thermochemical low-temperature cycle. In this paper, a solar system is integrated with a Mg-Cl cycle and a phase change CaO/CaCO3-CaCl2 thermochemical energy storage system (TCES). The heat generated by the solar tower is stored by the TCES in the charge mode. In the cases of low solar radiation, the TCES cycle stands in discharge mode and, if necessary, an auxiliary heat exchanger is utilized to provide the heat for the Mg-Cl cycle. The solar system is modeled by EES software and the other two cycles are simulated by Aspen Plus. Sensitivity and exergy analyses were performed for the system and reported along with the annual results of the whole system. The amount of 11.01 MW heat is stored in the charge mode and 9.536 MW is released in the discharge mode and 35.6 mol/s of hydrogen is acquired by the Mg-Cl cycle. The total exergy efficiencies of the TCES system and Mg-Cl cycle are 62.2% and 84.3%. The Mg-Cl cycle efficiency is enhanced due to the heat recovery of the internal streams and the TCES cycle efficiency is elevated due to the phase change process. The most exergy destroyer components of the TCES and Mg-Cl units belong to Carbonation and Electrolysis1 reactors with the value of 663.7 kW and 3747.4 kW, respectively. According to annual analysis, the most exergy destructions are related to the Electrolysis1 reactor, followed by solar system, which comprise 29.73% and 23.4% of total annual exergy destruction, respectively. Moreover, the annual system efficiency, exergy efficiency and solar fraction are 63.74%, 54.76, and 83.59%, respectively.</description><subject>Calcium carbonate</subject><subject>Calcium chloride</subject><subject>Carbonation</subject><subject>Discharge</subject><subject>Efficiency</subject><subject>Energy storage</subject><subject>Exergy</subject><subject>Heat</subject><subject>Heat exchangers</subject><subject>Heat recovery</subject><subject>Hydrogen</subject><subject>Hydrogen production</subject><subject>Low temperature</subject><subject>Mg-Cl cycle</subject><subject>Nuclear fuels</subject><subject>Phase change</subject><subject>Phase change calcium looping</subject><subject>Reactors</subject><subject>Solar radiation</subject><subject>Solar tower system</subject><subject>Thermochemical energy storage</subject><subject>Thermodynamics</subject><issn>0196-8904</issn><issn>1879-2227</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNqFUMtu2zAQJIoGiJvkFwICPctZkqJE3VoIfQRI4EvuxIZaPQyJdEm6hb-hPx2lTs-57AM7M4sZxm4FbAWI6m6_Je-CX9BvJUixFaLUWn9gG2HqppBS1h_ZBkRTFaaB8pJ9SmkPAEpDtWF_732mIWKmjj8ORTvz8dTFMJDnhxi6o8tT-Dc6Somj73iLu7sW250q1jpLnkeKS3AjLZPDmZOnOJx4yiHiQPwwYiLuRvTrkk4p08KPafIDT2HGyHP4Q_HtcM0uepwT3bz1K_b0_dtT-7N42P24b78-FE6VkIumBF0DSKSqewZlnK46UxNopaUUWIHWsjSidv2zULVSfY-IpGshqxplo67Y57Ps6urXkVK2-3CMfv1opTZCl8oYs6KqM8rFkFKk3h7itGA8WQH2NXe7t_9zt6-523PuK_HLmUirhd8TRZvctCKpmyK5bLswvSfxAtOmj-A</recordid><startdate>20211001</startdate><enddate>20211001</enddate><creator>Habibi, Roghayeh</creator><creator>Mehrpooya, Mehdi</creator><creator>Pourmoghadam, Peyman</creator><general>Elsevier Ltd</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope><scope>SOI</scope></search><sort><creationdate>20211001</creationdate><title>Integrated Mg-Cl hydrogen production process and CaO/CaCO3-CaCl2 thermochemical energy storage phase change system using solar tower system</title><author>Habibi, Roghayeh ; Mehrpooya, Mehdi ; Pourmoghadam, Peyman</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c340t-94057002ae6db038c56d87e0535221a605524817cfb13733ffaaae571267a293</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Calcium carbonate</topic><topic>Calcium chloride</topic><topic>Carbonation</topic><topic>Discharge</topic><topic>Efficiency</topic><topic>Energy storage</topic><topic>Exergy</topic><topic>Heat</topic><topic>Heat exchangers</topic><topic>Heat recovery</topic><topic>Hydrogen</topic><topic>Hydrogen production</topic><topic>Low temperature</topic><topic>Mg-Cl cycle</topic><topic>Nuclear fuels</topic><topic>Phase change</topic><topic>Phase change calcium looping</topic><topic>Reactors</topic><topic>Solar radiation</topic><topic>Solar tower system</topic><topic>Thermochemical energy storage</topic><topic>Thermodynamics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Habibi, Roghayeh</creatorcontrib><creatorcontrib>Mehrpooya, Mehdi</creatorcontrib><creatorcontrib>Pourmoghadam, Peyman</creatorcontrib><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Mechanical &amp; Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>Energy conversion and management</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Habibi, Roghayeh</au><au>Mehrpooya, Mehdi</au><au>Pourmoghadam, Peyman</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Integrated Mg-Cl hydrogen production process and CaO/CaCO3-CaCl2 thermochemical energy storage phase change system using solar tower system</atitle><jtitle>Energy conversion and management</jtitle><date>2021-10-01</date><risdate>2021</risdate><volume>245</volume><spage>114555</spage><pages>114555-</pages><artnum>114555</artnum><issn>0196-8904</issn><eissn>1879-2227</eissn><abstract>[Display omitted] •A hybrid phase change CaO/CaCO3-CaCl2 thermochemical energy storage system is investigated.•A Mg-Cl hydrogen production process is developed using solar thermal energy.•Total exergy efficiencies of the energy storage system and Mg-Cl cycle are 62.2% and 84.3%.•Annual system efficiency, exergy efficiency and solar fraction are 63.74%, 54.76, and 83.59%, respectively. Hydrogen has been considered as a clean and sustainable fuel to meet heat requirements. The Mg-Cl hydrogen production cycle has been introduced as a promising thermochemical low-temperature cycle. In this paper, a solar system is integrated with a Mg-Cl cycle and a phase change CaO/CaCO3-CaCl2 thermochemical energy storage system (TCES). The heat generated by the solar tower is stored by the TCES in the charge mode. In the cases of low solar radiation, the TCES cycle stands in discharge mode and, if necessary, an auxiliary heat exchanger is utilized to provide the heat for the Mg-Cl cycle. The solar system is modeled by EES software and the other two cycles are simulated by Aspen Plus. Sensitivity and exergy analyses were performed for the system and reported along with the annual results of the whole system. The amount of 11.01 MW heat is stored in the charge mode and 9.536 MW is released in the discharge mode and 35.6 mol/s of hydrogen is acquired by the Mg-Cl cycle. The total exergy efficiencies of the TCES system and Mg-Cl cycle are 62.2% and 84.3%. The Mg-Cl cycle efficiency is enhanced due to the heat recovery of the internal streams and the TCES cycle efficiency is elevated due to the phase change process. The most exergy destroyer components of the TCES and Mg-Cl units belong to Carbonation and Electrolysis1 reactors with the value of 663.7 kW and 3747.4 kW, respectively. According to annual analysis, the most exergy destructions are related to the Electrolysis1 reactor, followed by solar system, which comprise 29.73% and 23.4% of total annual exergy destruction, respectively. Moreover, the annual system efficiency, exergy efficiency and solar fraction are 63.74%, 54.76, and 83.59%, respectively.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.enconman.2021.114555</doi></addata></record>
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subjects Calcium carbonate
Calcium chloride
Carbonation
Discharge
Efficiency
Energy storage
Exergy
Heat
Heat exchangers
Heat recovery
Hydrogen
Hydrogen production
Low temperature
Mg-Cl cycle
Nuclear fuels
Phase change
Phase change calcium looping
Reactors
Solar radiation
Solar tower system
Thermochemical energy storage
Thermodynamics
title Integrated Mg-Cl hydrogen production process and CaO/CaCO3-CaCl2 thermochemical energy storage phase change system using solar tower system
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