Effect of additives on melting temperature and energy consumption of municipal solid waste incineration fly ash

This paper presents the melting temperature (MT) and energy consumption (EC) of model municipal solid waste incineration (MSWI) fly ash (FA) under the influence of calcium oxide (CaO), silicon dioxide (SiO2), aluminium oxide (Al2O3) and boron oxide (B2O3) based on thermochemistry simulations. Nine d...

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Veröffentlicht in:Waste management & research 2021-12, Vol.39 (12), p.1451-1458
Hauptverfasser: Gao, Jing, Dong, Changqing, Wang, Xiaodong, Zhu, Yanjun, Zhao, Ying, Lin, Yuan, Hu, Xiaoying
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container_end_page 1458
container_issue 12
container_start_page 1451
container_title Waste management & research
container_volume 39
creator Gao, Jing
Dong, Changqing
Wang, Xiaodong
Zhu, Yanjun
Zhao, Ying
Lin, Yuan
Hu, Xiaoying
description This paper presents the melting temperature (MT) and energy consumption (EC) of model municipal solid waste incineration (MSWI) fly ash (FA) under the influence of calcium oxide (CaO), silicon dioxide (SiO2), aluminium oxide (Al2O3) and boron oxide (B2O3) based on thermochemistry simulations. Nine different base-to-acid ratios (B/A) of raw FA have been explored. The results show that the effects of CaO, SiO2 and Al2O3 vary for different B/A ranges. SiO2 and Al2O3 play positive roles in decreasing the MT and EC of FA4–FA9 with high B/A (B/A: 2.61, 4.48, 6.43, 6.90, 8.32, 8.82). CaO plays a positive role in decreasing the MT and EC of FA1 and FA2 with low B/A (B/A: 0.22, 0.43). In FA3 (B/A: 1.22), the MT and EC of FA cannot be reduced by adding CaO, SiO2 and Al2O3. The addition of B2O3 cannot only further reduce the MT of FA, but also reduce the EC. B2O3 and SiO2 can work together to reduce the MT and EC when B/A is high (2.61–8.82), and SiO2 and B2O3 can be introduced into the FA by adding waste glass and other boron containing waste to realize the coordinated disposal of waste.
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Nine different base-to-acid ratios (B/A) of raw FA have been explored. The results show that the effects of CaO, SiO2 and Al2O3 vary for different B/A ranges. SiO2 and Al2O3 play positive roles in decreasing the MT and EC of FA4–FA9 with high B/A (B/A: 2.61, 4.48, 6.43, 6.90, 8.32, 8.82). CaO plays a positive role in decreasing the MT and EC of FA1 and FA2 with low B/A (B/A: 0.22, 0.43). In FA3 (B/A: 1.22), the MT and EC of FA cannot be reduced by adding CaO, SiO2 and Al2O3. The addition of B2O3 cannot only further reduce the MT of FA, but also reduce the EC. B2O3 and SiO2 can work together to reduce the MT and EC when B/A is high (2.61–8.82), and SiO2 and B2O3 can be introduced into the FA by adding waste glass and other boron containing waste to realize the coordinated disposal of waste.</description><identifier>ISSN: 0734-242X</identifier><identifier>EISSN: 1096-3669</identifier><identifier>DOI: 10.1177/0734242X20985610</identifier><identifier>PMID: 33499764</identifier><language>eng</language><publisher>London, England: SAGE Publications</publisher><subject>Additives ; Aluminum ; Aluminum oxide ; Boron ; Boron oxides ; Calcium oxide ; Combustion ; Energy consumption ; Fly ash ; Incineration ; Lime ; Melt temperature ; Melting ; Municipal solid waste ; Municipal waste management ; Silicon dioxide ; Solid waste management ; Thermochemistry ; Waste disposal</subject><ispartof>Waste management &amp; research, 2021-12, Vol.39 (12), p.1451-1458</ispartof><rights>The Author(s) 2021</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c365t-4a69ee62e3a0ecffc5ef709a1e8fa662ce6ca1db5ac6017016b09352f24dfdb43</citedby><cites>FETCH-LOGICAL-c365t-4a69ee62e3a0ecffc5ef709a1e8fa662ce6ca1db5ac6017016b09352f24dfdb43</cites><orcidid>0000-0001-6559-7889</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://journals.sagepub.com/doi/pdf/10.1177/0734242X20985610$$EPDF$$P50$$Gsage$$H</linktopdf><linktohtml>$$Uhttps://journals.sagepub.com/doi/10.1177/0734242X20985610$$EHTML$$P50$$Gsage$$H</linktohtml><link.rule.ids>314,780,784,21819,27924,27925,43621,43622</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/33499764$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Gao, Jing</creatorcontrib><creatorcontrib>Dong, Changqing</creatorcontrib><creatorcontrib>Wang, Xiaodong</creatorcontrib><creatorcontrib>Zhu, Yanjun</creatorcontrib><creatorcontrib>Zhao, Ying</creatorcontrib><creatorcontrib>Lin, Yuan</creatorcontrib><creatorcontrib>Hu, Xiaoying</creatorcontrib><title>Effect of additives on melting temperature and energy consumption of municipal solid waste incineration fly ash</title><title>Waste management &amp; research</title><addtitle>Waste Manag Res</addtitle><description>This paper presents the melting temperature (MT) and energy consumption (EC) of model municipal solid waste incineration (MSWI) fly ash (FA) under the influence of calcium oxide (CaO), silicon dioxide (SiO2), aluminium oxide (Al2O3) and boron oxide (B2O3) based on thermochemistry simulations. Nine different base-to-acid ratios (B/A) of raw FA have been explored. The results show that the effects of CaO, SiO2 and Al2O3 vary for different B/A ranges. SiO2 and Al2O3 play positive roles in decreasing the MT and EC of FA4–FA9 with high B/A (B/A: 2.61, 4.48, 6.43, 6.90, 8.32, 8.82). CaO plays a positive role in decreasing the MT and EC of FA1 and FA2 with low B/A (B/A: 0.22, 0.43). In FA3 (B/A: 1.22), the MT and EC of FA cannot be reduced by adding CaO, SiO2 and Al2O3. The addition of B2O3 cannot only further reduce the MT of FA, but also reduce the EC. 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research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Gao, Jing</au><au>Dong, Changqing</au><au>Wang, Xiaodong</au><au>Zhu, Yanjun</au><au>Zhao, Ying</au><au>Lin, Yuan</au><au>Hu, Xiaoying</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Effect of additives on melting temperature and energy consumption of municipal solid waste incineration fly ash</atitle><jtitle>Waste management &amp; research</jtitle><addtitle>Waste Manag Res</addtitle><date>2021-12-01</date><risdate>2021</risdate><volume>39</volume><issue>12</issue><spage>1451</spage><epage>1458</epage><pages>1451-1458</pages><issn>0734-242X</issn><eissn>1096-3669</eissn><abstract>This paper presents the melting temperature (MT) and energy consumption (EC) of model municipal solid waste incineration (MSWI) fly ash (FA) under the influence of calcium oxide (CaO), silicon dioxide (SiO2), aluminium oxide (Al2O3) and boron oxide (B2O3) based on thermochemistry simulations. Nine different base-to-acid ratios (B/A) of raw FA have been explored. The results show that the effects of CaO, SiO2 and Al2O3 vary for different B/A ranges. SiO2 and Al2O3 play positive roles in decreasing the MT and EC of FA4–FA9 with high B/A (B/A: 2.61, 4.48, 6.43, 6.90, 8.32, 8.82). CaO plays a positive role in decreasing the MT and EC of FA1 and FA2 with low B/A (B/A: 0.22, 0.43). In FA3 (B/A: 1.22), the MT and EC of FA cannot be reduced by adding CaO, SiO2 and Al2O3. The addition of B2O3 cannot only further reduce the MT of FA, but also reduce the EC. B2O3 and SiO2 can work together to reduce the MT and EC when B/A is high (2.61–8.82), and SiO2 and B2O3 can be introduced into the FA by adding waste glass and other boron containing waste to realize the coordinated disposal of waste.</abstract><cop>London, England</cop><pub>SAGE Publications</pub><pmid>33499764</pmid><doi>10.1177/0734242X20985610</doi><tpages>8</tpages><orcidid>https://orcid.org/0000-0001-6559-7889</orcidid></addata></record>
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source SAGE Complete A-Z List
subjects Additives
Aluminum
Aluminum oxide
Boron
Boron oxides
Calcium oxide
Combustion
Energy consumption
Fly ash
Incineration
Lime
Melt temperature
Melting
Municipal solid waste
Municipal waste management
Silicon dioxide
Solid waste management
Thermochemistry
Waste disposal
title Effect of additives on melting temperature and energy consumption of municipal solid waste incineration fly ash
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