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Oxy-combustion characteristics as a function of oxygen concentration and biomass co-firing ratio in a 0.1 MWth circulating fluidized bed combustion test-rig
Oxy-combustion with a circulating fluidized bed (Oxy-CFBC) can facilitate the separation of high CO2 concentration and reduce emissions by biomass co-firing. This study investigated Oxy-CFBC characteristics such as temperature, solid hold-up, flue gas concentrations including CO2, pollutant emission...
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Published in: | Energy (Oxford) 2020-04, Vol.196, p.117020, Article 117020 |
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creator | Nguyen, Hoang Khoi Moon, Ji-Hong Jo, Sung-Ho Park, Sung Jin Seo, Myung Won Ra, Ho Won Yoon, Sang-Jun Yoon, Sung-Min Song, Byungho Lee, Uendo Yang, Chang Won Mun, Tae-Young Lee, Jae-Goo |
description | Oxy-combustion with a circulating fluidized bed (Oxy-CFBC) can facilitate the separation of high CO2 concentration and reduce emissions by biomass co-firing. This study investigated Oxy-CFBC characteristics such as temperature, solid hold-up, flue gas concentrations including CO2, pollutant emissions (SO2, NO, and CO), combustion efficiency and ash properties (slagging, fouling index) with increasing input oxygen levels (21–29 vol%), and biomass co-firing ratios (50, 70, and 100 wt% with domestic wood pellet). The possibility of bio-energy carbon capture and storage for negative CO2 emission was also evaluated using a 0.1 MWth Oxy-CFBC test-rig. The results show that combustion stably achieved with at least 90 vol% CO2 in the flue gas. Compared to air-firing, oxy-firing (with 24 vol% oxygen) reduced pollutant emissions to 29.4% NO, 31.9% SO2 and 18.5% CO. Increasing the biomass co-firing from 50 to 100 wt% decreased the NO, SO2 and CO content from 19.2 mg/MJ to 16.1 mg/MJ, 92.8 mg/MJ to 25.0 mg/MJ, and 7.5 mg/MJ to 5.5 mg/MJ, respectively. In contrast to blends of sub-bituminous coal and lignite, negative CO2 emission (approximately −647 g/kWth) was predicted for oxy-combustion only biomass.
•Oxy-combustion with a 0.1 MWth CFB was operated.•Effect on the various O2 concentrations and biomass firing ratios investigated.•Stable shift from air-to oxy-fired easily achieved above 90% (dry) CO2 flue gas.•Oxy-fired NO and SO2 emissions lower than those of air-fired.•CO2 negative emission from biomass-only oxy-firing expected (−647 g CO2/kWth). |
doi_str_mv | 10.1016/j.energy.2020.117020 |
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•Oxy-combustion with a 0.1 MWth CFB was operated.•Effect on the various O2 concentrations and biomass firing ratios investigated.•Stable shift from air-to oxy-fired easily achieved above 90% (dry) CO2 flue gas.•Oxy-fired NO and SO2 emissions lower than those of air-fired.•CO2 negative emission from biomass-only oxy-firing expected (−647 g CO2/kWth).</description><identifier>ISSN: 0360-5442</identifier><identifier>EISSN: 1873-6785</identifier><identifier>DOI: 10.1016/j.energy.2020.117020</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Air pollution ; Ash ; Biomass ; Biomass burning ; Biomass co-firing ; Bituminous coal ; Carbon dioxide ; Carbon dioxide emissions ; Carbon sequestration ; CO2 ; Combustion ; Combustion efficiency ; Emission analysis ; Energy storage ; Firing ; Flue gas ; Fluidized bed combustion ; Fluidized beds ; Hardwoods ; Lignite ; O2 concentration ; Oxy-CFBC ; Oxygen ; Pollutant emissions ; Pollutants ; Pollution control ; Residential energy ; Slagging ; Sulfur dioxide</subject><ispartof>Energy (Oxford), 2020-04, Vol.196, p.117020, Article 117020</ispartof><rights>2020 Elsevier Ltd</rights><rights>Copyright Elsevier BV Apr 1, 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c334t-f0165196955830434e64deaa2f8ec6b04bb2a5cdfd6f3ef1d8023904073485683</citedby><cites>FETCH-LOGICAL-c334t-f0165196955830434e64deaa2f8ec6b04bb2a5cdfd6f3ef1d8023904073485683</cites><orcidid>0000-0001-5090-6992 ; 0000-0001-5669-9672 ; 0000-0002-7698-9981</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Nguyen, Hoang Khoi</creatorcontrib><creatorcontrib>Moon, Ji-Hong</creatorcontrib><creatorcontrib>Jo, Sung-Ho</creatorcontrib><creatorcontrib>Park, Sung Jin</creatorcontrib><creatorcontrib>Seo, Myung Won</creatorcontrib><creatorcontrib>Ra, Ho Won</creatorcontrib><creatorcontrib>Yoon, Sang-Jun</creatorcontrib><creatorcontrib>Yoon, Sung-Min</creatorcontrib><creatorcontrib>Song, Byungho</creatorcontrib><creatorcontrib>Lee, Uendo</creatorcontrib><creatorcontrib>Yang, Chang Won</creatorcontrib><creatorcontrib>Mun, Tae-Young</creatorcontrib><creatorcontrib>Lee, Jae-Goo</creatorcontrib><title>Oxy-combustion characteristics as a function of oxygen concentration and biomass co-firing ratio in a 0.1 MWth circulating fluidized bed combustion test-rig</title><title>Energy (Oxford)</title><description>Oxy-combustion with a circulating fluidized bed (Oxy-CFBC) can facilitate the separation of high CO2 concentration and reduce emissions by biomass co-firing. This study investigated Oxy-CFBC characteristics such as temperature, solid hold-up, flue gas concentrations including CO2, pollutant emissions (SO2, NO, and CO), combustion efficiency and ash properties (slagging, fouling index) with increasing input oxygen levels (21–29 vol%), and biomass co-firing ratios (50, 70, and 100 wt% with domestic wood pellet). The possibility of bio-energy carbon capture and storage for negative CO2 emission was also evaluated using a 0.1 MWth Oxy-CFBC test-rig. The results show that combustion stably achieved with at least 90 vol% CO2 in the flue gas. Compared to air-firing, oxy-firing (with 24 vol% oxygen) reduced pollutant emissions to 29.4% NO, 31.9% SO2 and 18.5% CO. Increasing the biomass co-firing from 50 to 100 wt% decreased the NO, SO2 and CO content from 19.2 mg/MJ to 16.1 mg/MJ, 92.8 mg/MJ to 25.0 mg/MJ, and 7.5 mg/MJ to 5.5 mg/MJ, respectively. In contrast to blends of sub-bituminous coal and lignite, negative CO2 emission (approximately −647 g/kWth) was predicted for oxy-combustion only biomass.
•Oxy-combustion with a 0.1 MWth CFB was operated.•Effect on the various O2 concentrations and biomass firing ratios investigated.•Stable shift from air-to oxy-fired easily achieved above 90% (dry) CO2 flue gas.•Oxy-fired NO and SO2 emissions lower than those of air-fired.•CO2 negative emission from biomass-only oxy-firing expected (−647 g CO2/kWth).</description><subject>Air pollution</subject><subject>Ash</subject><subject>Biomass</subject><subject>Biomass burning</subject><subject>Biomass co-firing</subject><subject>Bituminous coal</subject><subject>Carbon dioxide</subject><subject>Carbon dioxide emissions</subject><subject>Carbon sequestration</subject><subject>CO2</subject><subject>Combustion</subject><subject>Combustion efficiency</subject><subject>Emission analysis</subject><subject>Energy storage</subject><subject>Firing</subject><subject>Flue gas</subject><subject>Fluidized bed combustion</subject><subject>Fluidized beds</subject><subject>Hardwoods</subject><subject>Lignite</subject><subject>O2 concentration</subject><subject>Oxy-CFBC</subject><subject>Oxygen</subject><subject>Pollutant emissions</subject><subject>Pollutants</subject><subject>Pollution control</subject><subject>Residential energy</subject><subject>Slagging</subject><subject>Sulfur dioxide</subject><issn>0360-5442</issn><issn>1873-6785</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9UU1LAzEQDaJg_fgHHgKetyab7DZ7EUT8gooXxWPIZidtSrupya5Y_4vgb_GXOXY9eBIShsx7b2Yyj5ATzsac8fJsMYYW4mwzzlmOKT7BsENGXE1EVk5UsUtGTJQsK6TM98lBSgvGWKGqakQ-Ht42mQ2ruk-dDy21cxON7SB6fNtEDR7q-tZu0eBoeNvMAHmhtdB20Wzzpm1o7cPKpIRI5nz07YxuQeoRpjjV1-f9czen1kfbLxFBglv2vvHvgGK8f6boIHVZ9LMjsufMMsHxbzwkT9dXj5e32fTh5u7yYppZIWSXOVxCwauyKgolmBQSStmAMblTYMuaybrOTWEb15ROgOONYrmomGQTIVVRKnFIToe66xheemyuF6GPLbbUuZRcKcWFRJYcWDaGlCI4vY5-ZeJGc6Z_jNALPRihf4zQgxEoOx9kgD949RB1sh5wfY2PYDvdBP9_gW_pBpZX</recordid><startdate>20200401</startdate><enddate>20200401</enddate><creator>Nguyen, Hoang Khoi</creator><creator>Moon, Ji-Hong</creator><creator>Jo, Sung-Ho</creator><creator>Park, Sung Jin</creator><creator>Seo, Myung Won</creator><creator>Ra, Ho Won</creator><creator>Yoon, Sang-Jun</creator><creator>Yoon, Sung-Min</creator><creator>Song, Byungho</creator><creator>Lee, Uendo</creator><creator>Yang, Chang Won</creator><creator>Mun, Tae-Young</creator><creator>Lee, Jae-Goo</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>7ST</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>KR7</scope><scope>L7M</scope><scope>SOI</scope><orcidid>https://orcid.org/0000-0001-5090-6992</orcidid><orcidid>https://orcid.org/0000-0001-5669-9672</orcidid><orcidid>https://orcid.org/0000-0002-7698-9981</orcidid></search><sort><creationdate>20200401</creationdate><title>Oxy-combustion characteristics as a function of oxygen concentration and biomass co-firing ratio in a 0.1 MWth circulating fluidized bed combustion test-rig</title><author>Nguyen, Hoang Khoi ; Moon, Ji-Hong ; Jo, Sung-Ho ; Park, Sung Jin ; Seo, Myung Won ; Ra, Ho Won ; Yoon, Sang-Jun ; Yoon, Sung-Min ; Song, Byungho ; Lee, Uendo ; Yang, Chang Won ; Mun, Tae-Young ; Lee, Jae-Goo</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c334t-f0165196955830434e64deaa2f8ec6b04bb2a5cdfd6f3ef1d8023904073485683</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Air pollution</topic><topic>Ash</topic><topic>Biomass</topic><topic>Biomass burning</topic><topic>Biomass co-firing</topic><topic>Bituminous coal</topic><topic>Carbon dioxide</topic><topic>Carbon dioxide emissions</topic><topic>Carbon sequestration</topic><topic>CO2</topic><topic>Combustion</topic><topic>Combustion efficiency</topic><topic>Emission analysis</topic><topic>Energy storage</topic><topic>Firing</topic><topic>Flue gas</topic><topic>Fluidized bed combustion</topic><topic>Fluidized beds</topic><topic>Hardwoods</topic><topic>Lignite</topic><topic>O2 concentration</topic><topic>Oxy-CFBC</topic><topic>Oxygen</topic><topic>Pollutant emissions</topic><topic>Pollutants</topic><topic>Pollution control</topic><topic>Residential energy</topic><topic>Slagging</topic><topic>Sulfur dioxide</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Nguyen, Hoang Khoi</creatorcontrib><creatorcontrib>Moon, Ji-Hong</creatorcontrib><creatorcontrib>Jo, Sung-Ho</creatorcontrib><creatorcontrib>Park, Sung Jin</creatorcontrib><creatorcontrib>Seo, Myung Won</creatorcontrib><creatorcontrib>Ra, Ho Won</creatorcontrib><creatorcontrib>Yoon, Sang-Jun</creatorcontrib><creatorcontrib>Yoon, Sung-Min</creatorcontrib><creatorcontrib>Song, Byungho</creatorcontrib><creatorcontrib>Lee, Uendo</creatorcontrib><creatorcontrib>Yang, Chang Won</creatorcontrib><creatorcontrib>Mun, Tae-Young</creatorcontrib><creatorcontrib>Lee, Jae-Goo</creatorcontrib><collection>CrossRef</collection><collection>Electronics & Communications Abstracts</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</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>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>Energy (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Nguyen, Hoang Khoi</au><au>Moon, Ji-Hong</au><au>Jo, Sung-Ho</au><au>Park, Sung Jin</au><au>Seo, Myung Won</au><au>Ra, Ho Won</au><au>Yoon, Sang-Jun</au><au>Yoon, Sung-Min</au><au>Song, Byungho</au><au>Lee, Uendo</au><au>Yang, Chang Won</au><au>Mun, Tae-Young</au><au>Lee, Jae-Goo</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Oxy-combustion characteristics as a function of oxygen concentration and biomass co-firing ratio in a 0.1 MWth circulating fluidized bed combustion test-rig</atitle><jtitle>Energy (Oxford)</jtitle><date>2020-04-01</date><risdate>2020</risdate><volume>196</volume><spage>117020</spage><pages>117020-</pages><artnum>117020</artnum><issn>0360-5442</issn><eissn>1873-6785</eissn><abstract>Oxy-combustion with a circulating fluidized bed (Oxy-CFBC) can facilitate the separation of high CO2 concentration and reduce emissions by biomass co-firing. This study investigated Oxy-CFBC characteristics such as temperature, solid hold-up, flue gas concentrations including CO2, pollutant emissions (SO2, NO, and CO), combustion efficiency and ash properties (slagging, fouling index) with increasing input oxygen levels (21–29 vol%), and biomass co-firing ratios (50, 70, and 100 wt% with domestic wood pellet). The possibility of bio-energy carbon capture and storage for negative CO2 emission was also evaluated using a 0.1 MWth Oxy-CFBC test-rig. The results show that combustion stably achieved with at least 90 vol% CO2 in the flue gas. Compared to air-firing, oxy-firing (with 24 vol% oxygen) reduced pollutant emissions to 29.4% NO, 31.9% SO2 and 18.5% CO. Increasing the biomass co-firing from 50 to 100 wt% decreased the NO, SO2 and CO content from 19.2 mg/MJ to 16.1 mg/MJ, 92.8 mg/MJ to 25.0 mg/MJ, and 7.5 mg/MJ to 5.5 mg/MJ, respectively. In contrast to blends of sub-bituminous coal and lignite, negative CO2 emission (approximately −647 g/kWth) was predicted for oxy-combustion only biomass.
•Oxy-combustion with a 0.1 MWth CFB was operated.•Effect on the various O2 concentrations and biomass firing ratios investigated.•Stable shift from air-to oxy-fired easily achieved above 90% (dry) CO2 flue gas.•Oxy-fired NO and SO2 emissions lower than those of air-fired.•CO2 negative emission from biomass-only oxy-firing expected (−647 g CO2/kWth).</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.energy.2020.117020</doi><orcidid>https://orcid.org/0000-0001-5090-6992</orcidid><orcidid>https://orcid.org/0000-0001-5669-9672</orcidid><orcidid>https://orcid.org/0000-0002-7698-9981</orcidid></addata></record> |
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subjects | Air pollution Ash Biomass Biomass burning Biomass co-firing Bituminous coal Carbon dioxide Carbon dioxide emissions Carbon sequestration CO2 Combustion Combustion efficiency Emission analysis Energy storage Firing Flue gas Fluidized bed combustion Fluidized beds Hardwoods Lignite O2 concentration Oxy-CFBC Oxygen Pollutant emissions Pollutants Pollution control Residential energy Slagging Sulfur dioxide |
title | Oxy-combustion characteristics as a function of oxygen concentration and biomass co-firing ratio in a 0.1 MWth circulating fluidized bed combustion test-rig |
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