Kinetics and enthalpies of methane adsorption in microporous materials AX-21, MIL-101 (Cr) and TE7
•Kinetics of methane adsorption in activated carbons AX-21 and TE7 and MOF MIL-101 are analysed.•Mass transfer coefficients, effective diffusivities and activation energies are calculated.•Enthalpies are estimated with Clausius-Clapeyron equation for absolute and excess adsorption.•These are compare...
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description | •Kinetics of methane adsorption in activated carbons AX-21 and TE7 and MOF MIL-101 are analysed.•Mass transfer coefficients, effective diffusivities and activation energies are calculated.•Enthalpies are estimated with Clausius-Clapeyron equation for absolute and excess adsorption.•These are compared with differential calorimetry, with differences up to 3.5kJmol−1.
Methane is touted as a replacement for fossil fuels in transport applications due to its lower costs of production and cleaner combustion. Storage of methane is still a problem and different technologies have been considered, including compression and liquefaction. Adsorption in a porous material is a potential alternative for methane storage, as it can increase densities at moderate pressures and temperatures. For practical applications, in addition to the quantities stored and working capacities, it is important to equally consider aspects such as kinetics of storage and thermal management of the storage system. In this paper, the kinetics and enthalpies of adsorption of methane in activated carbons AX-21 and TE7, and metal-organic framework MIL-101 (Cr) are extracted from readily available gas sorption data. The adsorption kinetics at 300K and 325K are analysed and fitted with the linear driving force (LDF) model, and mass transfer coefficients (MTC) and effective diffusivities are estimated. The effective diffusivities have a range of values from 1.79×10−13m2s−1 for the MIL-101 (Cr) at 300K to 9.36×10−10m2s−1 for the TE7 at 325K. The activation energies for the effective diffusivities based on an Arrhenius-type temperature dependence are calculated as 7.42, 7.09 and 5.38kJmol−1 for the AX-21, the MIL-101 (Cr) and the TE7, respectively. The enthalpies of adsorption are calculated with the Clausius-Clapeyron equation and the differences observed when calculating these with excess and absolute amounts are presented and discussed, with the results showing that enthalpies can have up to 10% differences if using excess amounts instead of absolute quantities. The isosteric enthalpies are also compared with enthalpies at zero-coverage obtained from differential calorimetry experiments for the MIL-101 (Cr), and a ∼3.5kJmol−1 difference is observed, which underlines the importance of refining calculation methods and bridging the gap between direct and indirect methods for calculating enthalpies of adsorption. |
doi_str_mv | 10.1016/j.cherd.2021.03.003 |
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Methane is touted as a replacement for fossil fuels in transport applications due to its lower costs of production and cleaner combustion. Storage of methane is still a problem and different technologies have been considered, including compression and liquefaction. Adsorption in a porous material is a potential alternative for methane storage, as it can increase densities at moderate pressures and temperatures. For practical applications, in addition to the quantities stored and working capacities, it is important to equally consider aspects such as kinetics of storage and thermal management of the storage system. In this paper, the kinetics and enthalpies of adsorption of methane in activated carbons AX-21 and TE7, and metal-organic framework MIL-101 (Cr) are extracted from readily available gas sorption data. The adsorption kinetics at 300K and 325K are analysed and fitted with the linear driving force (LDF) model, and mass transfer coefficients (MTC) and effective diffusivities are estimated. The effective diffusivities have a range of values from 1.79×10−13m2s−1 for the MIL-101 (Cr) at 300K to 9.36×10−10m2s−1 for the TE7 at 325K. The activation energies for the effective diffusivities based on an Arrhenius-type temperature dependence are calculated as 7.42, 7.09 and 5.38kJmol−1 for the AX-21, the MIL-101 (Cr) and the TE7, respectively. The enthalpies of adsorption are calculated with the Clausius-Clapeyron equation and the differences observed when calculating these with excess and absolute amounts are presented and discussed, with the results showing that enthalpies can have up to 10% differences if using excess amounts instead of absolute quantities. The isosteric enthalpies are also compared with enthalpies at zero-coverage obtained from differential calorimetry experiments for the MIL-101 (Cr), and a ∼3.5kJmol−1 difference is observed, which underlines the importance of refining calculation methods and bridging the gap between direct and indirect methods for calculating enthalpies of adsorption.</description><identifier>ISSN: 0263-8762</identifier><identifier>EISSN: 1744-3563</identifier><identifier>DOI: 10.1016/j.cherd.2021.03.003</identifier><language>eng</language><publisher>Rugby: Elsevier Ltd</publisher><subject>Activated carbon ; Adsorption ; Chromium ; Enthalpies of adsorption ; Enthalpy ; Fossil fuels ; Kinetics ; Liquefaction ; Mass transfer ; Metal-organic frameworks ; Methane ; Methane adsorption ; Methane storage ; Porous materials ; Temperature ; Temperature dependence ; Thermal management ; Thermodynamics</subject><ispartof>Chemical engineering research & design, 2021-05, Vol.169, p.153-164</ispartof><rights>2021 Institution of Chemical Engineers</rights><rights>Copyright Elsevier Science Ltd. May 2021</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c376t-783785de7b42590ea054dfd0c907a4bbf125da3beca9ce267ec02a6e25e67e0e3</citedby><cites>FETCH-LOGICAL-c376t-783785de7b42590ea054dfd0c907a4bbf125da3beca9ce267ec02a6e25e67e0e3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.cherd.2021.03.003$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids></links><search><creatorcontrib>Bimbo, Nuno</creatorcontrib><creatorcontrib>Smith, Joseph P.</creatorcontrib><creatorcontrib>Aggarwal, Himanshu</creatorcontrib><creatorcontrib>Physick, Andrew J.</creatorcontrib><creatorcontrib>Pugsley, Adam</creatorcontrib><creatorcontrib>Barbour, Leonard J.</creatorcontrib><creatorcontrib>Ting, Valeska P.</creatorcontrib><creatorcontrib>Mays, Timothy J.</creatorcontrib><title>Kinetics and enthalpies of methane adsorption in microporous materials AX-21, MIL-101 (Cr) and TE7</title><title>Chemical engineering research & design</title><description>•Kinetics of methane adsorption in activated carbons AX-21 and TE7 and MOF MIL-101 are analysed.•Mass transfer coefficients, effective diffusivities and activation energies are calculated.•Enthalpies are estimated with Clausius-Clapeyron equation for absolute and excess adsorption.•These are compared with differential calorimetry, with differences up to 3.5kJmol−1.
Methane is touted as a replacement for fossil fuels in transport applications due to its lower costs of production and cleaner combustion. Storage of methane is still a problem and different technologies have been considered, including compression and liquefaction. Adsorption in a porous material is a potential alternative for methane storage, as it can increase densities at moderate pressures and temperatures. For practical applications, in addition to the quantities stored and working capacities, it is important to equally consider aspects such as kinetics of storage and thermal management of the storage system. In this paper, the kinetics and enthalpies of adsorption of methane in activated carbons AX-21 and TE7, and metal-organic framework MIL-101 (Cr) are extracted from readily available gas sorption data. The adsorption kinetics at 300K and 325K are analysed and fitted with the linear driving force (LDF) model, and mass transfer coefficients (MTC) and effective diffusivities are estimated. The effective diffusivities have a range of values from 1.79×10−13m2s−1 for the MIL-101 (Cr) at 300K to 9.36×10−10m2s−1 for the TE7 at 325K. The activation energies for the effective diffusivities based on an Arrhenius-type temperature dependence are calculated as 7.42, 7.09 and 5.38kJmol−1 for the AX-21, the MIL-101 (Cr) and the TE7, respectively. The enthalpies of adsorption are calculated with the Clausius-Clapeyron equation and the differences observed when calculating these with excess and absolute amounts are presented and discussed, with the results showing that enthalpies can have up to 10% differences if using excess amounts instead of absolute quantities. The isosteric enthalpies are also compared with enthalpies at zero-coverage obtained from differential calorimetry experiments for the MIL-101 (Cr), and a ∼3.5kJmol−1 difference is observed, which underlines the importance of refining calculation methods and bridging the gap between direct and indirect methods for calculating enthalpies of adsorption.</description><subject>Activated carbon</subject><subject>Adsorption</subject><subject>Chromium</subject><subject>Enthalpies of adsorption</subject><subject>Enthalpy</subject><subject>Fossil fuels</subject><subject>Kinetics</subject><subject>Liquefaction</subject><subject>Mass transfer</subject><subject>Metal-organic frameworks</subject><subject>Methane</subject><subject>Methane adsorption</subject><subject>Methane storage</subject><subject>Porous materials</subject><subject>Temperature</subject><subject>Temperature dependence</subject><subject>Thermal management</subject><subject>Thermodynamics</subject><issn>0263-8762</issn><issn>1744-3563</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNp9UE1LAzEQDaJgrf4CLwEvCu46SXaT9uChFD-KFS8K3kI2mcWUdrMmW8F_b2w9e5oZ5r038x4h5wxKBkzerEr7gdGVHDgrQZQA4oCMmKqqQtRSHJIRcCmKiZL8mJyktAKAvJ2MSPPkOxy8TdR0jmI3fJh17zHR0NIN5qlDalwKsR986Kjv6MbbGPoQwzbRjRkwerNOdPZecHZNnxfLIn9EL-fxaqf4eqdOyVGbIXj2V8fk7f7udf5YLF8eFvPZsrBCyaFQE6EmtUPVVLyeAhqoK9c6sFNQpmqalvHaGdGgNVOLXCq0wI1EXmPuAcWYXOx1-xg-t5gGvQrb2OWTmteSMZCVYhkl9qjsIqWIre6j35j4rRno3zD1Su_C1L9hahA6h5lZt3sWZgNfHqNO1mNn0fmIdtAu-H_5P6ngfHs</recordid><startdate>202105</startdate><enddate>202105</enddate><creator>Bimbo, Nuno</creator><creator>Smith, Joseph P.</creator><creator>Aggarwal, Himanshu</creator><creator>Physick, Andrew J.</creator><creator>Pugsley, Adam</creator><creator>Barbour, Leonard J.</creator><creator>Ting, Valeska P.</creator><creator>Mays, Timothy J.</creator><general>Elsevier Ltd</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8FD</scope><scope>JG9</scope></search><sort><creationdate>202105</creationdate><title>Kinetics and enthalpies of methane adsorption in microporous materials AX-21, MIL-101 (Cr) and TE7</title><author>Bimbo, Nuno ; Smith, Joseph P. ; Aggarwal, Himanshu ; Physick, Andrew J. ; Pugsley, Adam ; Barbour, Leonard J. ; Ting, Valeska P. ; Mays, Timothy J.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c376t-783785de7b42590ea054dfd0c907a4bbf125da3beca9ce267ec02a6e25e67e0e3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Activated carbon</topic><topic>Adsorption</topic><topic>Chromium</topic><topic>Enthalpies of adsorption</topic><topic>Enthalpy</topic><topic>Fossil fuels</topic><topic>Kinetics</topic><topic>Liquefaction</topic><topic>Mass transfer</topic><topic>Metal-organic frameworks</topic><topic>Methane</topic><topic>Methane adsorption</topic><topic>Methane storage</topic><topic>Porous materials</topic><topic>Temperature</topic><topic>Temperature dependence</topic><topic>Thermal management</topic><topic>Thermodynamics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Bimbo, Nuno</creatorcontrib><creatorcontrib>Smith, Joseph P.</creatorcontrib><creatorcontrib>Aggarwal, Himanshu</creatorcontrib><creatorcontrib>Physick, Andrew J.</creatorcontrib><creatorcontrib>Pugsley, Adam</creatorcontrib><creatorcontrib>Barbour, Leonard J.</creatorcontrib><creatorcontrib>Ting, Valeska P.</creatorcontrib><creatorcontrib>Mays, Timothy J.</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Chemical engineering research & design</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Bimbo, Nuno</au><au>Smith, Joseph P.</au><au>Aggarwal, Himanshu</au><au>Physick, Andrew J.</au><au>Pugsley, Adam</au><au>Barbour, Leonard J.</au><au>Ting, Valeska P.</au><au>Mays, Timothy J.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetics and enthalpies of methane adsorption in microporous materials AX-21, MIL-101 (Cr) and TE7</atitle><jtitle>Chemical engineering research & design</jtitle><date>2021-05</date><risdate>2021</risdate><volume>169</volume><spage>153</spage><epage>164</epage><pages>153-164</pages><issn>0263-8762</issn><eissn>1744-3563</eissn><abstract>•Kinetics of methane adsorption in activated carbons AX-21 and TE7 and MOF MIL-101 are analysed.•Mass transfer coefficients, effective diffusivities and activation energies are calculated.•Enthalpies are estimated with Clausius-Clapeyron equation for absolute and excess adsorption.•These are compared with differential calorimetry, with differences up to 3.5kJmol−1.
Methane is touted as a replacement for fossil fuels in transport applications due to its lower costs of production and cleaner combustion. Storage of methane is still a problem and different technologies have been considered, including compression and liquefaction. Adsorption in a porous material is a potential alternative for methane storage, as it can increase densities at moderate pressures and temperatures. For practical applications, in addition to the quantities stored and working capacities, it is important to equally consider aspects such as kinetics of storage and thermal management of the storage system. In this paper, the kinetics and enthalpies of adsorption of methane in activated carbons AX-21 and TE7, and metal-organic framework MIL-101 (Cr) are extracted from readily available gas sorption data. The adsorption kinetics at 300K and 325K are analysed and fitted with the linear driving force (LDF) model, and mass transfer coefficients (MTC) and effective diffusivities are estimated. The effective diffusivities have a range of values from 1.79×10−13m2s−1 for the MIL-101 (Cr) at 300K to 9.36×10−10m2s−1 for the TE7 at 325K. The activation energies for the effective diffusivities based on an Arrhenius-type temperature dependence are calculated as 7.42, 7.09 and 5.38kJmol−1 for the AX-21, the MIL-101 (Cr) and the TE7, respectively. The enthalpies of adsorption are calculated with the Clausius-Clapeyron equation and the differences observed when calculating these with excess and absolute amounts are presented and discussed, with the results showing that enthalpies can have up to 10% differences if using excess amounts instead of absolute quantities. The isosteric enthalpies are also compared with enthalpies at zero-coverage obtained from differential calorimetry experiments for the MIL-101 (Cr), and a ∼3.5kJmol−1 difference is observed, which underlines the importance of refining calculation methods and bridging the gap between direct and indirect methods for calculating enthalpies of adsorption.</abstract><cop>Rugby</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.cherd.2021.03.003</doi><tpages>12</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Activated carbon Adsorption Chromium Enthalpies of adsorption Enthalpy Fossil fuels Kinetics Liquefaction Mass transfer Metal-organic frameworks Methane Methane adsorption Methane storage Porous materials Temperature Temperature dependence Thermal management Thermodynamics |
title | Kinetics and enthalpies of methane adsorption in microporous materials AX-21, MIL-101 (Cr) and TE7 |
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