Separation of CO2/N2 mixture by vacuum pressure swing adsorption (VPSA) using zeolite 13X type and carbon molecular sieve adsorbents
Separation of carbon dioxide in flue gases from the combustion equipment is one of the most serious concerns for industries and especially for the power plants which are the main producers of this pollutant gas. From the various separation methods, vacuum pressure swing adsorption (VPSA) process is...
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| Veröffentlicht in: | Heat and mass transfer 2020, Vol.56 (6), p.1985-1994 |
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| container_end_page | 1994 |
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| container_issue | 6 |
| container_start_page | 1985 |
| container_title | Heat and mass transfer |
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| creator | Alibolandi, Mehdi Sadrameli, Seyed Mojtaba Rezaee, Fatemeh Darian, Jafar Towfighi |
| description | Separation of carbon dioxide in flue gases from the combustion equipment is one of the most serious concerns for industries and especially for the power plants which are the main producers of this pollutant gas. From the various separation methods, vacuum pressure swing adsorption (VPSA) process is attracted interest due to its lower energy consumption and high efficiency. A VPSA process was studied for the separation of a mixture of CO
2
/N
2
(80% N
2
and 20% CO
2
). Experiments were performed in an eight-step, four-bed setup using zeolite 13X and carbon molecular sieve (CMS) as adsorbents. Experimental measurements by the bench-scale system have been obtained in a pressure range of 2.7–4.7 bar, cycle times of 360–600 s, the product flow rate of 1–3 (lit/min), and temperature 30 °C. The effects of pressure, cycle time, and product flow rate were investigated. With using 560 s for a cycle time at 3.7 bar, the maximum purity of 97.6% was obtained for zeolite 13X adsorbent. |
| doi_str_mv | 10.1007/s00231-020-02823-y |
| format | Article |
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2
/N
2
(80% N
2
and 20% CO
2
). Experiments were performed in an eight-step, four-bed setup using zeolite 13X and carbon molecular sieve (CMS) as adsorbents. Experimental measurements by the bench-scale system have been obtained in a pressure range of 2.7–4.7 bar, cycle times of 360–600 s, the product flow rate of 1–3 (lit/min), and temperature 30 °C. The effects of pressure, cycle time, and product flow rate were investigated. With using 560 s for a cycle time at 3.7 bar, the maximum purity of 97.6% was obtained for zeolite 13X adsorbent.</description><identifier>ISSN: 0947-7411</identifier><identifier>EISSN: 1432-1181</identifier><identifier>DOI: 10.1007/s00231-020-02823-y</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Adsorbents ; Carbon dioxide ; Cycle time ; Electric power generation ; Energy consumption ; Engineering ; Engineering Thermodynamics ; Flow velocity ; Flue gas ; Heat and Mass Transfer ; Industrial Chemistry/Chemical Engineering ; Industrial plants ; Molecular sieves ; Original Article ; Pollutants ; Power plants ; Pressure effects ; Pressure swing adsorption ; Separation ; Thermodynamics ; Zeolites</subject><ispartof>Heat and mass transfer, 2020, Vol.56 (6), p.1985-1994</ispartof><rights>Springer-Verlag GmbH Germany, part of Springer Nature 2020</rights><rights>Springer-Verlag GmbH Germany, part of Springer Nature 2020.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c271y-2b371fd3346ca06738d327f9051782c32ad8f85a65f28f4efd936b36544beb083</citedby><cites>FETCH-LOGICAL-c271y-2b371fd3346ca06738d327f9051782c32ad8f85a65f28f4efd936b36544beb083</cites><orcidid>0000-0002-9732-7012</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s00231-020-02823-y$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s00231-020-02823-y$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,776,780,27901,27902,41464,42533,51294</link.rule.ids></links><search><creatorcontrib>Alibolandi, Mehdi</creatorcontrib><creatorcontrib>Sadrameli, Seyed Mojtaba</creatorcontrib><creatorcontrib>Rezaee, Fatemeh</creatorcontrib><creatorcontrib>Darian, Jafar Towfighi</creatorcontrib><title>Separation of CO2/N2 mixture by vacuum pressure swing adsorption (VPSA) using zeolite 13X type and carbon molecular sieve adsorbents</title><title>Heat and mass transfer</title><addtitle>Heat Mass Transfer</addtitle><description>Separation of carbon dioxide in flue gases from the combustion equipment is one of the most serious concerns for industries and especially for the power plants which are the main producers of this pollutant gas. From the various separation methods, vacuum pressure swing adsorption (VPSA) process is attracted interest due to its lower energy consumption and high efficiency. A VPSA process was studied for the separation of a mixture of CO
2
/N
2
(80% N
2
and 20% CO
2
). Experiments were performed in an eight-step, four-bed setup using zeolite 13X and carbon molecular sieve (CMS) as adsorbents. Experimental measurements by the bench-scale system have been obtained in a pressure range of 2.7–4.7 bar, cycle times of 360–600 s, the product flow rate of 1–3 (lit/min), and temperature 30 °C. The effects of pressure, cycle time, and product flow rate were investigated. With using 560 s for a cycle time at 3.7 bar, the maximum purity of 97.6% was obtained for zeolite 13X adsorbent.</description><subject>Adsorbents</subject><subject>Carbon dioxide</subject><subject>Cycle time</subject><subject>Electric power generation</subject><subject>Energy consumption</subject><subject>Engineering</subject><subject>Engineering Thermodynamics</subject><subject>Flow velocity</subject><subject>Flue gas</subject><subject>Heat and Mass Transfer</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Industrial plants</subject><subject>Molecular sieves</subject><subject>Original Article</subject><subject>Pollutants</subject><subject>Power plants</subject><subject>Pressure effects</subject><subject>Pressure swing adsorption</subject><subject>Separation</subject><subject>Thermodynamics</subject><subject>Zeolites</subject><issn>0947-7411</issn><issn>1432-1181</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9kF1LwzAUhoMoOKd_wKuAN3pRl6822eUYfsFwwlS8C2mbjI62qUk7rdf-cLNV8M6Lw4HD874HHgDOMbrGCPGJR4hQHCGCwghCo_4AjDCjJMJY4EMwQlPGI84wPgYn3m8CnjBCR-B7pRvlVFvYGloD50syeSSwKj7bzmmY9nCrsq6rYOO097uT_yjqNVS5t67Zpy5fn1azK9j53f1L27JoNcT0DbZ9o6Gqc5gplwawsqXOulI56Au91UNHquvWn4Ijo0qvz373GLzc3jzP76PF8u5hPltEGeG4j0hKOTY5pSzJFEo4FTkl3ExRjLkgGSUqF0bEKokNEYZpk09pktIkZizVKRJ0DC6G3sbZ9077Vm5s5-rwUhKGEoo5ZyxQZKAyZ7132sjGFZVyvcRI7mzLwbYMtuXetuxDiA4hH-B6rd1f9T-pH7TogxE</recordid><startdate>2020</startdate><enddate>2020</enddate><creator>Alibolandi, Mehdi</creator><creator>Sadrameli, Seyed Mojtaba</creator><creator>Rezaee, Fatemeh</creator><creator>Darian, Jafar Towfighi</creator><general>Springer Berlin Heidelberg</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0002-9732-7012</orcidid></search><sort><creationdate>2020</creationdate><title>Separation of CO2/N2 mixture by vacuum pressure swing adsorption (VPSA) using zeolite 13X type and carbon molecular sieve adsorbents</title><author>Alibolandi, Mehdi ; Sadrameli, Seyed Mojtaba ; Rezaee, Fatemeh ; Darian, Jafar Towfighi</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c271y-2b371fd3346ca06738d327f9051782c32ad8f85a65f28f4efd936b36544beb083</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Adsorbents</topic><topic>Carbon dioxide</topic><topic>Cycle time</topic><topic>Electric power generation</topic><topic>Energy consumption</topic><topic>Engineering</topic><topic>Engineering Thermodynamics</topic><topic>Flow velocity</topic><topic>Flue gas</topic><topic>Heat and Mass Transfer</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Industrial plants</topic><topic>Molecular sieves</topic><topic>Original Article</topic><topic>Pollutants</topic><topic>Power plants</topic><topic>Pressure effects</topic><topic>Pressure swing adsorption</topic><topic>Separation</topic><topic>Thermodynamics</topic><topic>Zeolites</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Alibolandi, Mehdi</creatorcontrib><creatorcontrib>Sadrameli, Seyed Mojtaba</creatorcontrib><creatorcontrib>Rezaee, Fatemeh</creatorcontrib><creatorcontrib>Darian, Jafar Towfighi</creatorcontrib><collection>CrossRef</collection><jtitle>Heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Alibolandi, Mehdi</au><au>Sadrameli, Seyed Mojtaba</au><au>Rezaee, Fatemeh</au><au>Darian, Jafar Towfighi</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Separation of CO2/N2 mixture by vacuum pressure swing adsorption (VPSA) using zeolite 13X type and carbon molecular sieve adsorbents</atitle><jtitle>Heat and mass transfer</jtitle><stitle>Heat Mass Transfer</stitle><date>2020</date><risdate>2020</risdate><volume>56</volume><issue>6</issue><spage>1985</spage><epage>1994</epage><pages>1985-1994</pages><issn>0947-7411</issn><eissn>1432-1181</eissn><abstract>Separation of carbon dioxide in flue gases from the combustion equipment is one of the most serious concerns for industries and especially for the power plants which are the main producers of this pollutant gas. From the various separation methods, vacuum pressure swing adsorption (VPSA) process is attracted interest due to its lower energy consumption and high efficiency. A VPSA process was studied for the separation of a mixture of CO
2
/N
2
(80% N
2
and 20% CO
2
). Experiments were performed in an eight-step, four-bed setup using zeolite 13X and carbon molecular sieve (CMS) as adsorbents. Experimental measurements by the bench-scale system have been obtained in a pressure range of 2.7–4.7 bar, cycle times of 360–600 s, the product flow rate of 1–3 (lit/min), and temperature 30 °C. The effects of pressure, cycle time, and product flow rate were investigated. With using 560 s for a cycle time at 3.7 bar, the maximum purity of 97.6% was obtained for zeolite 13X adsorbent.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s00231-020-02823-y</doi><tpages>10</tpages><orcidid>https://orcid.org/0000-0002-9732-7012</orcidid></addata></record> |
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| ispartof | Heat and mass transfer, 2020, Vol.56 (6), p.1985-1994 |
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| source | SpringerLink Journals - AutoHoldings |
| subjects | Adsorbents Carbon dioxide Cycle time Electric power generation Energy consumption Engineering Engineering Thermodynamics Flow velocity Flue gas Heat and Mass Transfer Industrial Chemistry/Chemical Engineering Industrial plants Molecular sieves Original Article Pollutants Power plants Pressure effects Pressure swing adsorption Separation Thermodynamics Zeolites |
| title | Separation of CO2/N2 mixture by vacuum pressure swing adsorption (VPSA) using zeolite 13X type and carbon molecular sieve adsorbents |
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