Decomposition of high concentration benzene (produced in paper and painting industries) and its byproducts, methane and carbon dioxide, using plate gliding arc
High concentration benzene production in paper and painting industries is a restrictive problem in production line of companies. In this study, removal of high concentrated benzene produced in painting companies was investigated using a Plate Gliding Arc (PGA) reactor. Decomposition of methane and c...
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Veröffentlicht in: | Journal of environmental health science and engineering 2019-12, Vol.17 (2), p.549-560 |
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creator | Rad, Rezvan Hosseini Khani, Mohammad Reza Mehdikia, Hamed Shafiei, Mojtaba Shokri, Babak |
description | High concentration benzene production in paper and painting industries is a restrictive problem in production line of companies. In this study, removal of high concentrated benzene produced in painting companies was investigated using a Plate Gliding Arc (PGA) reactor. Decomposition of methane and carbon dioxide as the most predominate byproducts of benzene decomposition was also studied using (PGA) reactor. The effect of several parameters such as input power, feed gas flow rate, type of carrier gas, and [CH
4
/CO
2
] flow ratio was studied by two series of experiments. The results show significant conversion (>70%) of high concentration benzene (74000ppm) without using any catalyst. Selectivity of CO
2
and CO was 88% and 10% respectively showing complete oxidation of benzene. The maximum conversion of CH
4
and CO
2
reached 52% and 69%, respectively by using optimum ratio of 3:4. The main results of this study proved removal of high concentration benzene using a low-energy-density reactor. Furthermore, an optimum value for efficient conversion of methane and carbon dioxide was achieved and the energy density of the PGA reactor was evaluated, which shows a good promise for industrial applications. |
doi_str_mv | 10.1007/s40201-019-00369-8 |
format | Article |
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4
/CO
2
] flow ratio was studied by two series of experiments. The results show significant conversion (>70%) of high concentration benzene (74000ppm) without using any catalyst. Selectivity of CO
2
and CO was 88% and 10% respectively showing complete oxidation of benzene. The maximum conversion of CH
4
and CO
2
reached 52% and 69%, respectively by using optimum ratio of 3:4. The main results of this study proved removal of high concentration benzene using a low-energy-density reactor. Furthermore, an optimum value for efficient conversion of methane and carbon dioxide was achieved and the energy density of the PGA reactor was evaluated, which shows a good promise for industrial applications.</description><identifier>ISSN: 2052-336X</identifier><identifier>EISSN: 2052-336X</identifier><identifier>DOI: 10.1007/s40201-019-00369-8</identifier><identifier>PMID: 32030133</identifier><language>eng</language><publisher>Cham: Springer International Publishing</publisher><subject>Benzene ; Byproducts ; Carbon dioxide ; Carrier gases ; Catalysts ; Conversion ; Decomposition ; Decomposition reactions ; Earth and Environmental Science ; Environment ; Environmental Economics ; Environmental Engineering/Biotechnology ; Environmental Health ; Environmental Law/Policy/Ecojustice ; Flow velocity ; Flux density ; Gas flow ; Gliding ; Hydrocarbons ; Industrial applications ; Methane ; Oxidation ; Quality of Life Research ; Reactors ; Research Article ; Selectivity ; Waste Management/Waste Technology</subject><ispartof>Journal of environmental health science and engineering, 2019-12, Vol.17 (2), p.549-560</ispartof><rights>Springer Nature Switzerland AG 2019</rights><rights>Springer Nature Switzerland AG 2019.</rights><rights>2019© Springer Nature Switzerland AG 2019</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c441t-5da7d5ef4e3467ab864f309c944bd5c3fc292fda487aa1e3da0e339a6c1aab0b3</citedby><cites>FETCH-LOGICAL-c441t-5da7d5ef4e3467ab864f309c944bd5c3fc292fda487aa1e3da0e339a6c1aab0b3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC6985433/pdf/$$EPDF$$P50$$Gpubmedcentral$$H</linktopdf><linktohtml>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC6985433/$$EHTML$$P50$$Gpubmedcentral$$H</linktohtml><link.rule.ids>230,314,723,776,780,881,27901,27902,41464,42533,51294,53766,53768</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/32030133$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Rad, Rezvan Hosseini</creatorcontrib><creatorcontrib>Khani, Mohammad Reza</creatorcontrib><creatorcontrib>Mehdikia, Hamed</creatorcontrib><creatorcontrib>Shafiei, Mojtaba</creatorcontrib><creatorcontrib>Shokri, Babak</creatorcontrib><title>Decomposition of high concentration benzene (produced in paper and painting industries) and its byproducts, methane and carbon dioxide, using plate gliding arc</title><title>Journal of environmental health science and engineering</title><addtitle>J Environ Health Sci Engineer</addtitle><addtitle>J Environ Health Sci Eng</addtitle><description>High concentration benzene production in paper and painting industries is a restrictive problem in production line of companies. In this study, removal of high concentrated benzene produced in painting companies was investigated using a Plate Gliding Arc (PGA) reactor. Decomposition of methane and carbon dioxide as the most predominate byproducts of benzene decomposition was also studied using (PGA) reactor. The effect of several parameters such as input power, feed gas flow rate, type of carrier gas, and [CH
4
/CO
2
] flow ratio was studied by two series of experiments. The results show significant conversion (>70%) of high concentration benzene (74000ppm) without using any catalyst. Selectivity of CO
2
and CO was 88% and 10% respectively showing complete oxidation of benzene. The maximum conversion of CH
4
and CO
2
reached 52% and 69%, respectively by using optimum ratio of 3:4. The main results of this study proved removal of high concentration benzene using a low-energy-density reactor. Furthermore, an optimum value for efficient conversion of methane and carbon dioxide was achieved and the energy density of the PGA reactor was evaluated, which shows a good promise for industrial applications.</description><subject>Benzene</subject><subject>Byproducts</subject><subject>Carbon dioxide</subject><subject>Carrier gases</subject><subject>Catalysts</subject><subject>Conversion</subject><subject>Decomposition</subject><subject>Decomposition reactions</subject><subject>Earth and Environmental Science</subject><subject>Environment</subject><subject>Environmental Economics</subject><subject>Environmental Engineering/Biotechnology</subject><subject>Environmental Health</subject><subject>Environmental Law/Policy/Ecojustice</subject><subject>Flow velocity</subject><subject>Flux density</subject><subject>Gas flow</subject><subject>Gliding</subject><subject>Hydrocarbons</subject><subject>Industrial applications</subject><subject>Methane</subject><subject>Oxidation</subject><subject>Quality of Life Research</subject><subject>Reactors</subject><subject>Research Article</subject><subject>Selectivity</subject><subject>Waste Management/Waste Technology</subject><issn>2052-336X</issn><issn>2052-336X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp9ks1u1TAQhSMEolXpC7BAltgUqQHb4_xtkFD5lSqxAYmd5diTXFe5drAdRHkZXhXnppTCgpXHc44_e-RTFI8Zfc4obV5EQTllJWVdSSnUXdneK445rXgJUH-5f6c-Kk5jvKKUMgrQdtXD4gg4BcoAjoufr1H7_eyjTdY74geys-OOaO80uhTUoduj-4EOydkcvFk0GmIdmdWMgShncmVdsm7MXbPEFCzGZwfBpkj66-1Qiudkj2mnMmfVtAp9Rhvrv1uD52SJK2GeVEIyTtasOxX0o-LBoKaIpzfrSfH57ZtPF-_Ly4_vPly8uiy1ECyVlVGNqXAQCKJuVN_WYgDa6U6I3lQaBs07Phgl2kYphmAURYBO1Zop1dMeToqXG3de-j2abfhJzsHuVbiWXln5t-LsTo7-m6y7thIAGXB2Awj-64Ixyb2NGqcpD-yXKDlUvAZesTZbn_5jvfJLcHm87BK16BqgTXbxzaWDjzHgcPsYRuUaAblFQOYIyEME5Ip-cneM2yO_PzwbYDPELLkRw5-7_4P9Bb4LwLU</recordid><startdate>20191201</startdate><enddate>20191201</enddate><creator>Rad, Rezvan Hosseini</creator><creator>Khani, Mohammad Reza</creator><creator>Mehdikia, Hamed</creator><creator>Shafiei, Mojtaba</creator><creator>Shokri, Babak</creator><general>Springer International Publishing</general><general>BioMed Central</general><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>K9.</scope><scope>SOI</scope><scope>7X8</scope><scope>5PM</scope></search><sort><creationdate>20191201</creationdate><title>Decomposition of high concentration benzene (produced in paper and painting industries) and its byproducts, methane and carbon dioxide, using plate gliding arc</title><author>Rad, Rezvan Hosseini ; Khani, Mohammad Reza ; Mehdikia, Hamed ; Shafiei, Mojtaba ; Shokri, Babak</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c441t-5da7d5ef4e3467ab864f309c944bd5c3fc292fda487aa1e3da0e339a6c1aab0b3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Benzene</topic><topic>Byproducts</topic><topic>Carbon dioxide</topic><topic>Carrier gases</topic><topic>Catalysts</topic><topic>Conversion</topic><topic>Decomposition</topic><topic>Decomposition reactions</topic><topic>Earth and Environmental Science</topic><topic>Environment</topic><topic>Environmental Economics</topic><topic>Environmental Engineering/Biotechnology</topic><topic>Environmental Health</topic><topic>Environmental Law/Policy/Ecojustice</topic><topic>Flow velocity</topic><topic>Flux density</topic><topic>Gas flow</topic><topic>Gliding</topic><topic>Hydrocarbons</topic><topic>Industrial applications</topic><topic>Methane</topic><topic>Oxidation</topic><topic>Quality of Life Research</topic><topic>Reactors</topic><topic>Research Article</topic><topic>Selectivity</topic><topic>Waste Management/Waste Technology</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Rad, Rezvan Hosseini</creatorcontrib><creatorcontrib>Khani, Mohammad Reza</creatorcontrib><creatorcontrib>Mehdikia, Hamed</creatorcontrib><creatorcontrib>Shafiei, Mojtaba</creatorcontrib><creatorcontrib>Shokri, Babak</creatorcontrib><collection>PubMed</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ProQuest Health & Medical Complete (Alumni)</collection><collection>Environment Abstracts</collection><collection>MEDLINE - Academic</collection><collection>PubMed Central (Full Participant titles)</collection><jtitle>Journal of environmental health science and engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Rad, Rezvan Hosseini</au><au>Khani, Mohammad Reza</au><au>Mehdikia, Hamed</au><au>Shafiei, Mojtaba</au><au>Shokri, Babak</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Decomposition of high concentration benzene (produced in paper and painting industries) and its byproducts, methane and carbon dioxide, using plate gliding arc</atitle><jtitle>Journal of environmental health science and engineering</jtitle><stitle>J Environ Health Sci Engineer</stitle><addtitle>J Environ Health Sci Eng</addtitle><date>2019-12-01</date><risdate>2019</risdate><volume>17</volume><issue>2</issue><spage>549</spage><epage>560</epage><pages>549-560</pages><issn>2052-336X</issn><eissn>2052-336X</eissn><abstract>High concentration benzene production in paper and painting industries is a restrictive problem in production line of companies. In this study, removal of high concentrated benzene produced in painting companies was investigated using a Plate Gliding Arc (PGA) reactor. Decomposition of methane and carbon dioxide as the most predominate byproducts of benzene decomposition was also studied using (PGA) reactor. The effect of several parameters such as input power, feed gas flow rate, type of carrier gas, and [CH
4
/CO
2
] flow ratio was studied by two series of experiments. The results show significant conversion (>70%) of high concentration benzene (74000ppm) without using any catalyst. Selectivity of CO
2
and CO was 88% and 10% respectively showing complete oxidation of benzene. The maximum conversion of CH
4
and CO
2
reached 52% and 69%, respectively by using optimum ratio of 3:4. The main results of this study proved removal of high concentration benzene using a low-energy-density reactor. Furthermore, an optimum value for efficient conversion of methane and carbon dioxide was achieved and the energy density of the PGA reactor was evaluated, which shows a good promise for industrial applications.</abstract><cop>Cham</cop><pub>Springer International Publishing</pub><pmid>32030133</pmid><doi>10.1007/s40201-019-00369-8</doi><tpages>12</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Benzene Byproducts Carbon dioxide Carrier gases Catalysts Conversion Decomposition Decomposition reactions Earth and Environmental Science Environment Environmental Economics Environmental Engineering/Biotechnology Environmental Health Environmental Law/Policy/Ecojustice Flow velocity Flux density Gas flow Gliding Hydrocarbons Industrial applications Methane Oxidation Quality of Life Research Reactors Research Article Selectivity Waste Management/Waste Technology |
title | Decomposition of high concentration benzene (produced in paper and painting industries) and its byproducts, methane and carbon dioxide, using plate gliding arc |
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