Carbon dioxide absorption with aqueous amine solutions promoted by piperazine and 1-methylpiperazine in a rotating zigzag bed
•Rotating zigzag bed (RZB) applied to CO2 absorption with aqueous amine solution.•Diethylenetriamine with piperazine or 1-methylpiperazine (1-MPZ) used as absorbent.•Piperazine exhibited better promoting effect than 1-MPZ for CO2 absorption.•RZB showed better CO2 absorption and mass transfer effect...
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creator | Liu, Zhibang Esmaeili, Arash Zhang, Hanxiao Xiao, Hao Yun, Jimmy Shao, Lei |
description | •Rotating zigzag bed (RZB) applied to CO2 absorption with aqueous amine solution.•Diethylenetriamine with piperazine or 1-methylpiperazine (1-MPZ) used as absorbent.•Piperazine exhibited better promoting effect than 1-MPZ for CO2 absorption.•RZB showed better CO2 absorption and mass transfer effect than rotating packed bed.
In order to overcome the drawback of short liquid resistance time in rotating packed bed (RPB), a multi-stage rotating zigzag bed (RZB) was employed to enhance carbon dioxide (CO2) absorption process with blended aqueous amine solutions containing diethylenetriamine (DETA) + piperazine (PZ) or DETA + 1-methylpiperazine (1-MPZ) as absorbents. The effects of different operating parameters on the CO2 absorption efficiency, overall gas-phase volumetric mass transfer coefficient (KGa) and height of mass transfer unit in the RZB were investigated. Experimental results indicated that increase of the promoter concentration, lean solution flow rate and rotational speed were conducive to gas–liquid mass transfer and CO2 absorption. It was found that both PZ and 1-MPZ were effective promoters, while PZ exhibited better performance. Meanwhile, comparison of CO2 absorption performance between one stage and two stages revealed that two stages had higher CO2 absorption efficiency due to extended residence time of absorbents and CO2 in the RZB. A comparison with RPB demonstrated that the RZB could achieve higher mass transfer and CO2 absorption efficiencies with smaller rotor volume and less absorbent consumption. The maximum CO2 absorption efficiency and KGa reached 99.3% at a gas flow rate of 1.5 m3/h and 7.43 kmol/kPa m3 h at an inlet gas CO2 concentration of 2% respectively in the RZB with DETA + PZ system, suggesting that RZB may be an effective device for CO2 absorption. |
doi_str_mv | 10.1016/j.fuel.2021.121165 |
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In order to overcome the drawback of short liquid resistance time in rotating packed bed (RPB), a multi-stage rotating zigzag bed (RZB) was employed to enhance carbon dioxide (CO2) absorption process with blended aqueous amine solutions containing diethylenetriamine (DETA) + piperazine (PZ) or DETA + 1-methylpiperazine (1-MPZ) as absorbents. The effects of different operating parameters on the CO2 absorption efficiency, overall gas-phase volumetric mass transfer coefficient (KGa) and height of mass transfer unit in the RZB were investigated. Experimental results indicated that increase of the promoter concentration, lean solution flow rate and rotational speed were conducive to gas–liquid mass transfer and CO2 absorption. It was found that both PZ and 1-MPZ were effective promoters, while PZ exhibited better performance. Meanwhile, comparison of CO2 absorption performance between one stage and two stages revealed that two stages had higher CO2 absorption efficiency due to extended residence time of absorbents and CO2 in the RZB. A comparison with RPB demonstrated that the RZB could achieve higher mass transfer and CO2 absorption efficiencies with smaller rotor volume and less absorbent consumption. The maximum CO2 absorption efficiency and KGa reached 99.3% at a gas flow rate of 1.5 m3/h and 7.43 kmol/kPa m3 h at an inlet gas CO2 concentration of 2% respectively in the RZB with DETA + PZ system, suggesting that RZB may be an effective device for CO2 absorption.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2021.121165</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Absorbents ; Absorption ; Absorption efficiency ; Blended aqueous amine solution ; Carbon dioxide ; Diethylene triamine ; Efficiency ; Flow rates ; Flow velocity ; Fluid flow ; Gas flow ; Gas-liquid mass transfer ; Mass transfer ; Packed beds ; Piperazine ; Rotating liquids ; Rotating zigzag bed ; Rotation</subject><ispartof>Fuel (Guildford), 2021-10, Vol.302, p.121165, Article 121165</ispartof><rights>2021 Elsevier Ltd</rights><rights>Copyright Elsevier BV Oct 15, 2021</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c328t-2b8e33474de81266086121bc4e5d4f7cde748462414556530369ec274c69ba6c3</citedby><cites>FETCH-LOGICAL-c328t-2b8e33474de81266086121bc4e5d4f7cde748462414556530369ec274c69ba6c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0016236121010449$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65534</link.rule.ids></links><search><creatorcontrib>Liu, Zhibang</creatorcontrib><creatorcontrib>Esmaeili, Arash</creatorcontrib><creatorcontrib>Zhang, Hanxiao</creatorcontrib><creatorcontrib>Xiao, Hao</creatorcontrib><creatorcontrib>Yun, Jimmy</creatorcontrib><creatorcontrib>Shao, Lei</creatorcontrib><title>Carbon dioxide absorption with aqueous amine solutions promoted by piperazine and 1-methylpiperazine in a rotating zigzag bed</title><title>Fuel (Guildford)</title><description>•Rotating zigzag bed (RZB) applied to CO2 absorption with aqueous amine solution.•Diethylenetriamine with piperazine or 1-methylpiperazine (1-MPZ) used as absorbent.•Piperazine exhibited better promoting effect than 1-MPZ for CO2 absorption.•RZB showed better CO2 absorption and mass transfer effect than rotating packed bed.
In order to overcome the drawback of short liquid resistance time in rotating packed bed (RPB), a multi-stage rotating zigzag bed (RZB) was employed to enhance carbon dioxide (CO2) absorption process with blended aqueous amine solutions containing diethylenetriamine (DETA) + piperazine (PZ) or DETA + 1-methylpiperazine (1-MPZ) as absorbents. The effects of different operating parameters on the CO2 absorption efficiency, overall gas-phase volumetric mass transfer coefficient (KGa) and height of mass transfer unit in the RZB were investigated. Experimental results indicated that increase of the promoter concentration, lean solution flow rate and rotational speed were conducive to gas–liquid mass transfer and CO2 absorption. It was found that both PZ and 1-MPZ were effective promoters, while PZ exhibited better performance. Meanwhile, comparison of CO2 absorption performance between one stage and two stages revealed that two stages had higher CO2 absorption efficiency due to extended residence time of absorbents and CO2 in the RZB. A comparison with RPB demonstrated that the RZB could achieve higher mass transfer and CO2 absorption efficiencies with smaller rotor volume and less absorbent consumption. The maximum CO2 absorption efficiency and KGa reached 99.3% at a gas flow rate of 1.5 m3/h and 7.43 kmol/kPa m3 h at an inlet gas CO2 concentration of 2% respectively in the RZB with DETA + PZ system, suggesting that RZB may be an effective device for CO2 absorption.</description><subject>Absorbents</subject><subject>Absorption</subject><subject>Absorption efficiency</subject><subject>Blended aqueous amine solution</subject><subject>Carbon dioxide</subject><subject>Diethylene triamine</subject><subject>Efficiency</subject><subject>Flow rates</subject><subject>Flow velocity</subject><subject>Fluid flow</subject><subject>Gas flow</subject><subject>Gas-liquid mass transfer</subject><subject>Mass transfer</subject><subject>Packed beds</subject><subject>Piperazine</subject><subject>Rotating liquids</subject><subject>Rotating zigzag bed</subject><subject>Rotation</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNp9UE1LAzEUDKJgrf4BTwHPu-Zrs1vwIsUvELzoOWST1zal3axJVm3B_26WevDk6cG8mfdmBqFLSkpKqLxel4sBNiUjjJaUUSqrIzShTc2Lmlb8GE1IZhWMS3qKzmJcE0LqphIT9D3XofUdts5_OQtYt9GHPrkMfbq0wvp9AD9ErLeuAxz9Zhh3EffBb30Ci9sd7l0PQe9Hgu4spsUW0mq3-QO7DmscfNLJdUu8d8u9XuIW7Dk6WehNhIvfOUVv93ev88fi-eXhaX77XBjOmlSwtgHORS0sNJRJSRqZQ7ZGQGXFojYWatEIyQQVVSUrTricgWG1MHLWamn4FF0d7mbbOVBMau2H0OWXilWSUiIawjKLHVgm-BgDLFQf3FaHnaJEjTWrtRprVmPN6lBzFt0cRJD9fzgIKhoHnQHrApikrHf_yX8ABfuHPg</recordid><startdate>20211015</startdate><enddate>20211015</enddate><creator>Liu, Zhibang</creator><creator>Esmaeili, Arash</creator><creator>Zhang, Hanxiao</creator><creator>Xiao, Hao</creator><creator>Yun, Jimmy</creator><creator>Shao, Lei</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope></search><sort><creationdate>20211015</creationdate><title>Carbon dioxide absorption with aqueous amine solutions promoted by piperazine and 1-methylpiperazine in a rotating zigzag bed</title><author>Liu, Zhibang ; Esmaeili, Arash ; Zhang, Hanxiao ; Xiao, Hao ; Yun, Jimmy ; Shao, Lei</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c328t-2b8e33474de81266086121bc4e5d4f7cde748462414556530369ec274c69ba6c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Absorbents</topic><topic>Absorption</topic><topic>Absorption efficiency</topic><topic>Blended aqueous amine solution</topic><topic>Carbon dioxide</topic><topic>Diethylene triamine</topic><topic>Efficiency</topic><topic>Flow rates</topic><topic>Flow velocity</topic><topic>Fluid flow</topic><topic>Gas flow</topic><topic>Gas-liquid mass transfer</topic><topic>Mass transfer</topic><topic>Packed beds</topic><topic>Piperazine</topic><topic>Rotating liquids</topic><topic>Rotating zigzag bed</topic><topic>Rotation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Liu, Zhibang</creatorcontrib><creatorcontrib>Esmaeili, Arash</creatorcontrib><creatorcontrib>Zhang, Hanxiao</creatorcontrib><creatorcontrib>Xiao, Hao</creatorcontrib><creatorcontrib>Yun, Jimmy</creatorcontrib><creatorcontrib>Shao, Lei</creatorcontrib><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><jtitle>Fuel (Guildford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Liu, Zhibang</au><au>Esmaeili, Arash</au><au>Zhang, Hanxiao</au><au>Xiao, Hao</au><au>Yun, Jimmy</au><au>Shao, Lei</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Carbon dioxide absorption with aqueous amine solutions promoted by piperazine and 1-methylpiperazine in a rotating zigzag bed</atitle><jtitle>Fuel (Guildford)</jtitle><date>2021-10-15</date><risdate>2021</risdate><volume>302</volume><spage>121165</spage><pages>121165-</pages><artnum>121165</artnum><issn>0016-2361</issn><eissn>1873-7153</eissn><abstract>•Rotating zigzag bed (RZB) applied to CO2 absorption with aqueous amine solution.•Diethylenetriamine with piperazine or 1-methylpiperazine (1-MPZ) used as absorbent.•Piperazine exhibited better promoting effect than 1-MPZ for CO2 absorption.•RZB showed better CO2 absorption and mass transfer effect than rotating packed bed.
In order to overcome the drawback of short liquid resistance time in rotating packed bed (RPB), a multi-stage rotating zigzag bed (RZB) was employed to enhance carbon dioxide (CO2) absorption process with blended aqueous amine solutions containing diethylenetriamine (DETA) + piperazine (PZ) or DETA + 1-methylpiperazine (1-MPZ) as absorbents. The effects of different operating parameters on the CO2 absorption efficiency, overall gas-phase volumetric mass transfer coefficient (KGa) and height of mass transfer unit in the RZB were investigated. Experimental results indicated that increase of the promoter concentration, lean solution flow rate and rotational speed were conducive to gas–liquid mass transfer and CO2 absorption. It was found that both PZ and 1-MPZ were effective promoters, while PZ exhibited better performance. Meanwhile, comparison of CO2 absorption performance between one stage and two stages revealed that two stages had higher CO2 absorption efficiency due to extended residence time of absorbents and CO2 in the RZB. A comparison with RPB demonstrated that the RZB could achieve higher mass transfer and CO2 absorption efficiencies with smaller rotor volume and less absorbent consumption. The maximum CO2 absorption efficiency and KGa reached 99.3% at a gas flow rate of 1.5 m3/h and 7.43 kmol/kPa m3 h at an inlet gas CO2 concentration of 2% respectively in the RZB with DETA + PZ system, suggesting that RZB may be an effective device for CO2 absorption.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2021.121165</doi></addata></record> |
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subjects | Absorbents Absorption Absorption efficiency Blended aqueous amine solution Carbon dioxide Diethylene triamine Efficiency Flow rates Flow velocity Fluid flow Gas flow Gas-liquid mass transfer Mass transfer Packed beds Piperazine Rotating liquids Rotating zigzag bed Rotation |
title | Carbon dioxide absorption with aqueous amine solutions promoted by piperazine and 1-methylpiperazine in a rotating zigzag bed |
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