De- and rehydration of Ca(OH)2 in a reactor with direct heat transfer for thermo-chemical heat storage. Part B: Validation of model
► 2D model of the reactor to compare the experimental and simulated results. ► Validation of model. ► Good agreement regarding heat transfer, integral reaction rate and maximum temperatures. ► Good agreement regarding the temperature profiles after adaptation of the reaction rate. Heat storage techn...
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| Veröffentlicht in: | Chemical engineering research & design 2013-05, Vol.91 (5), p.865-873 |
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| creator | Schaube, F. Utz, I. Wörner, A. Müller-Steinhagen, H. |
| description | ► 2D model of the reactor to compare the experimental and simulated results. ► Validation of model. ► Good agreement regarding heat transfer, integral reaction rate and maximum temperatures. ► Good agreement regarding the temperature profiles after adaptation of the reaction rate.
Heat storage technologies are used to improve energy efficiency of power plants and recovery of process heat. Storing thermal energy by reversible thermo-chemical reactions offers a promising option for high storage capacities especially at high temperatures. Due to its low material cost the use of the gas–solid reaction Ca(OH)2⇌CaO+H2O has been suggested. In Part A of this work the thermal behavior of a reactor with direct heat transfer was experimentally investigated. In this part a two-dimensional model is applied for the specified system. The experimental and simulated results during the exothermic hydration are discussed in order to confirm the validity of the model. The model is validated regarding heat transfer, integral reaction rate and maximum temperatures. In addition, an adaptation of the kinetic equation is proposed in order to take into account rate-limiting effects due to agglomeration in the powder bed. |
| doi_str_mv | 10.1016/j.cherd.2013.02.019 |
| format | Article |
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Heat storage technologies are used to improve energy efficiency of power plants and recovery of process heat. Storing thermal energy by reversible thermo-chemical reactions offers a promising option for high storage capacities especially at high temperatures. Due to its low material cost the use of the gas–solid reaction Ca(OH)2⇌CaO+H2O has been suggested. In Part A of this work the thermal behavior of a reactor with direct heat transfer was experimentally investigated. In this part a two-dimensional model is applied for the specified system. The experimental and simulated results during the exothermic hydration are discussed in order to confirm the validity of the model. The model is validated regarding heat transfer, integral reaction rate and maximum temperatures. In addition, an adaptation of the kinetic equation is proposed in order to take into account rate-limiting effects due to agglomeration in the powder bed.</description><identifier>ISSN: 0263-8762</identifier><identifier>DOI: 10.1016/j.cherd.2013.02.019</identifier><language>eng</language><publisher>Elsevier B.V</publisher><subject>Agglomeration ; Calcium hydroxide ; Calcium oxide ; CFD ; Computer simulation ; Direct contact ; Electric power generation ; Energy management ; Gas–solid reaction ; Heat storage ; Heat transfer ; Hydration ; Reactors ; Thermo-chemical heat storage</subject><ispartof>Chemical engineering research & design, 2013-05, Vol.91 (5), p.865-873</ispartof><rights>2013 The Institution of Chemical Engineers</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c321t-b5ff89053255f4282dc09c78f707634bc5f139bb0b63c4d5105d330f9b0e4c2f3</citedby><cites>FETCH-LOGICAL-c321t-b5ff89053255f4282dc09c78f707634bc5f139bb0b63c4d5105d330f9b0e4c2f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0263876213000828$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3536,27903,27904,65309</link.rule.ids></links><search><creatorcontrib>Schaube, F.</creatorcontrib><creatorcontrib>Utz, I.</creatorcontrib><creatorcontrib>Wörner, A.</creatorcontrib><creatorcontrib>Müller-Steinhagen, H.</creatorcontrib><title>De- and rehydration of Ca(OH)2 in a reactor with direct heat transfer for thermo-chemical heat storage. Part B: Validation of model</title><title>Chemical engineering research & design</title><description>► 2D model of the reactor to compare the experimental and simulated results. ► Validation of model. ► Good agreement regarding heat transfer, integral reaction rate and maximum temperatures. ► Good agreement regarding the temperature profiles after adaptation of the reaction rate.
Heat storage technologies are used to improve energy efficiency of power plants and recovery of process heat. Storing thermal energy by reversible thermo-chemical reactions offers a promising option for high storage capacities especially at high temperatures. Due to its low material cost the use of the gas–solid reaction Ca(OH)2⇌CaO+H2O has been suggested. In Part A of this work the thermal behavior of a reactor with direct heat transfer was experimentally investigated. In this part a two-dimensional model is applied for the specified system. The experimental and simulated results during the exothermic hydration are discussed in order to confirm the validity of the model. The model is validated regarding heat transfer, integral reaction rate and maximum temperatures. In addition, an adaptation of the kinetic equation is proposed in order to take into account rate-limiting effects due to agglomeration in the powder bed.</description><subject>Agglomeration</subject><subject>Calcium hydroxide</subject><subject>Calcium oxide</subject><subject>CFD</subject><subject>Computer simulation</subject><subject>Direct contact</subject><subject>Electric power generation</subject><subject>Energy management</subject><subject>Gas–solid reaction</subject><subject>Heat storage</subject><subject>Heat transfer</subject><subject>Hydration</subject><subject>Reactors</subject><subject>Thermo-chemical heat storage</subject><issn>0263-8762</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNqFkUFP3DAQhXNoJSjwC3rxEQ5Jx3YSJ0g90KWwlZCWA3C1HHvMepXEYJtWnPnjGIJ6bE9zmPfN07xXFF8pVBRo-21X6S0GUzGgvAJWAe0_FfvAWl52omV7xZcYdwBARd3tFy_nWBI1GxJw-2yCSs7PxFuyUseb9QkjbiYq75ROPpA_Lm2JcQF1IltUiaSg5mgxEJu3KdtOvszuk9NqXBQxc-oeK3KtQiI_TsmdGp35azN5g-Nh8dmqMeLRxzwobi9-3qzW5dXm8tfq7KrUnNFUDo21XQ8NZ01ja9Yxo6HXorMCRMvrQTeW8n4YYGi5rk1DoTGcg-0HwFozyw-K4-XuQ_CPTxiTnFzUOI5qRv8UJRXQi45Swf4v5SIH2rC6y1K-SHXwMQa08iG4SYVnSUG-NSJ38r0R-daIBCZzI5n6vlCYH_7tMMioHc4al3il8e6f_CsWlJYg</recordid><startdate>201305</startdate><enddate>201305</enddate><creator>Schaube, F.</creator><creator>Utz, I.</creator><creator>Wörner, A.</creator><creator>Müller-Steinhagen, H.</creator><general>Elsevier B.V</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SU</scope><scope>7TB</scope><scope>7U5</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>L7M</scope><scope>7SR</scope><scope>8BQ</scope><scope>JG9</scope></search><sort><creationdate>201305</creationdate><title>De- and rehydration of Ca(OH)2 in a reactor with direct heat transfer for thermo-chemical heat storage. 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Part B: Validation of model</atitle><jtitle>Chemical engineering research & design</jtitle><date>2013-05</date><risdate>2013</risdate><volume>91</volume><issue>5</issue><spage>865</spage><epage>873</epage><pages>865-873</pages><issn>0263-8762</issn><abstract>► 2D model of the reactor to compare the experimental and simulated results. ► Validation of model. ► Good agreement regarding heat transfer, integral reaction rate and maximum temperatures. ► Good agreement regarding the temperature profiles after adaptation of the reaction rate.
Heat storage technologies are used to improve energy efficiency of power plants and recovery of process heat. Storing thermal energy by reversible thermo-chemical reactions offers a promising option for high storage capacities especially at high temperatures. Due to its low material cost the use of the gas–solid reaction Ca(OH)2⇌CaO+H2O has been suggested. In Part A of this work the thermal behavior of a reactor with direct heat transfer was experimentally investigated. In this part a two-dimensional model is applied for the specified system. The experimental and simulated results during the exothermic hydration are discussed in order to confirm the validity of the model. The model is validated regarding heat transfer, integral reaction rate and maximum temperatures. In addition, an adaptation of the kinetic equation is proposed in order to take into account rate-limiting effects due to agglomeration in the powder bed.</abstract><pub>Elsevier B.V</pub><doi>10.1016/j.cherd.2013.02.019</doi><tpages>9</tpages></addata></record> |
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| ispartof | Chemical engineering research & design, 2013-05, Vol.91 (5), p.865-873 |
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| language | eng |
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| source | Elsevier ScienceDirect Journals |
| subjects | Agglomeration Calcium hydroxide Calcium oxide CFD Computer simulation Direct contact Electric power generation Energy management Gas–solid reaction Heat storage Heat transfer Hydration Reactors Thermo-chemical heat storage |
| title | De- and rehydration of Ca(OH)2 in a reactor with direct heat transfer for thermo-chemical heat storage. Part B: Validation of model |
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