Study on pyrolysis of oil sludge with microalgae residue additive
The pyrolysis of oil sludge (OS) with microalgae residue (MR) additive was conducted with a TGA and a tube furnace. The pyrolysis process of OS with the MR additive can be divided into three stages: 1) water evaporation, 2) the release of light groups of hydrocarbon compounds, the cracking of heavy...
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Veröffentlicht in: | Canadian journal of chemical engineering 2018-09, Vol.96 (9), p.1919-1925 |
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container_issue | 9 |
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container_title | Canadian journal of chemical engineering |
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creator | Gong, Zhiqiang Wang, Zhentong Wang, Zhenbo Du, Aixun Fang, Peiwen Sun, Zhiqian Li, Xiaoyu |
description | The pyrolysis of oil sludge (OS) with microalgae residue (MR) additive was conducted with a TGA and a tube furnace. The pyrolysis process of OS with the MR additive can be divided into three stages: 1) water evaporation, 2) the release of light groups of hydrocarbon compounds, the cracking of heavy groups, and carbon decomposition, and 3) minerals decomposition. With the MR addition ratio increasing, the yield of oil and gas increased, and oil to gas ratio increased during OS pyrolysis. The MR addition improved the quality of pyrolysis oil and gas from OS pyrolysis. The proportion of light oil increased from 38 % with a 5 % MR addition ratio to 45 % with a 30 % addition ratio. Major components of pyrolysis gas included H2, CO, CO2, and CxHy. With the increase of the MR blending ratio, CO and CO2 contents increased, while H2 and CxHy contents decreased. Adding MR favoured the transformation of heavy hydrocarbons (C6+), resulting in a high content of light hydrocarbons. This work can help promote massive synergistic treatment of OS and microalgae biomass. |
doi_str_mv | 10.1002/cjce.23143 |
format | Article |
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The pyrolysis process of OS with the MR additive can be divided into three stages: 1) water evaporation, 2) the release of light groups of hydrocarbon compounds, the cracking of heavy groups, and carbon decomposition, and 3) minerals decomposition. With the MR addition ratio increasing, the yield of oil and gas increased, and oil to gas ratio increased during OS pyrolysis. The MR addition improved the quality of pyrolysis oil and gas from OS pyrolysis. The proportion of light oil increased from 38 % with a 5 % MR addition ratio to 45 % with a 30 % addition ratio. Major components of pyrolysis gas included H2, CO, CO2, and CxHy. With the increase of the MR blending ratio, CO and CO2 contents increased, while H2 and CxHy contents decreased. Adding MR favoured the transformation of heavy hydrocarbons (C6+), resulting in a high content of light hydrocarbons. This work can help promote massive synergistic treatment of OS and microalgae biomass.</description><identifier>ISSN: 0008-4034</identifier><identifier>EISSN: 1939-019X</identifier><identifier>DOI: 10.1002/cjce.23143</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc</publisher><subject>Algae ; Carbon dioxide ; Carbon monoxide ; co‐pyrolysis ; Decomposition ; Hydrocarbons ; microalgae residue ; oil sludge ; Pyrolysis ; Sludge ; tube furnace ; Tube furnaces</subject><ispartof>Canadian journal of chemical engineering, 2018-09, Vol.96 (9), p.1919-1925</ispartof><rights>2018 Canadian Society for Chemical Engineering</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3383-b6862ea66b2b632c2cb3d2c6179b063af53ba6451a6223da7c42a917e18317cf3</citedby><cites>FETCH-LOGICAL-c3383-b6862ea66b2b632c2cb3d2c6179b063af53ba6451a6223da7c42a917e18317cf3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fcjce.23143$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fcjce.23143$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids></links><search><creatorcontrib>Gong, Zhiqiang</creatorcontrib><creatorcontrib>Wang, Zhentong</creatorcontrib><creatorcontrib>Wang, Zhenbo</creatorcontrib><creatorcontrib>Du, Aixun</creatorcontrib><creatorcontrib>Fang, Peiwen</creatorcontrib><creatorcontrib>Sun, Zhiqian</creatorcontrib><creatorcontrib>Li, Xiaoyu</creatorcontrib><title>Study on pyrolysis of oil sludge with microalgae residue additive</title><title>Canadian journal of chemical engineering</title><description>The pyrolysis of oil sludge (OS) with microalgae residue (MR) additive was conducted with a TGA and a tube furnace. The pyrolysis process of OS with the MR additive can be divided into three stages: 1) water evaporation, 2) the release of light groups of hydrocarbon compounds, the cracking of heavy groups, and carbon decomposition, and 3) minerals decomposition. With the MR addition ratio increasing, the yield of oil and gas increased, and oil to gas ratio increased during OS pyrolysis. The MR addition improved the quality of pyrolysis oil and gas from OS pyrolysis. The proportion of light oil increased from 38 % with a 5 % MR addition ratio to 45 % with a 30 % addition ratio. Major components of pyrolysis gas included H2, CO, CO2, and CxHy. With the increase of the MR blending ratio, CO and CO2 contents increased, while H2 and CxHy contents decreased. Adding MR favoured the transformation of heavy hydrocarbons (C6+), resulting in a high content of light hydrocarbons. This work can help promote massive synergistic treatment of OS and microalgae biomass.</description><subject>Algae</subject><subject>Carbon dioxide</subject><subject>Carbon monoxide</subject><subject>co‐pyrolysis</subject><subject>Decomposition</subject><subject>Hydrocarbons</subject><subject>microalgae residue</subject><subject>oil sludge</subject><subject>Pyrolysis</subject><subject>Sludge</subject><subject>tube furnace</subject><subject>Tube furnaces</subject><issn>0008-4034</issn><issn>1939-019X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp9kF1LwzAUhoMoOKc3_oKAd0JnTk6XtpejzC8GXqjgXUiTdGZ0y0xaR_-9nfXaq8MLzznv4SHkGtgMGON3eqPtjCOkeEImUGCRMCg-TsmEMZYnKcP0nFzEuBkiZylMyOK17UxP_Y7u--CbPrpIfU29a2hsOrO29ODaT7p1OnjVrJWlwUZnOkuVMa513_aSnNWqifbqb07J-_3yrXxMVi8PT-VilWjEHJNK5IJbJUTFK4Fcc12h4VpAVlRMoKrnWCmRzkEJztGoTKdcFZBZyBEyXeOU3Ix398F_dTa2cuO7sBsqJWd5ijnDAgbqdqSGf2MMtpb74LYq9BKYPCqSR0XyV9EAwwgfXGP7f0hZPpfLcecHup1n5g</recordid><startdate>201809</startdate><enddate>201809</enddate><creator>Gong, Zhiqiang</creator><creator>Wang, Zhentong</creator><creator>Wang, Zhenbo</creator><creator>Du, Aixun</creator><creator>Fang, Peiwen</creator><creator>Sun, Zhiqian</creator><creator>Li, Xiaoyu</creator><general>Wiley Subscription Services, Inc</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>201809</creationdate><title>Study on pyrolysis of oil sludge with microalgae residue additive</title><author>Gong, Zhiqiang ; Wang, Zhentong ; Wang, Zhenbo ; Du, Aixun ; Fang, Peiwen ; Sun, Zhiqian ; Li, Xiaoyu</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3383-b6862ea66b2b632c2cb3d2c6179b063af53ba6451a6223da7c42a917e18317cf3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Algae</topic><topic>Carbon dioxide</topic><topic>Carbon monoxide</topic><topic>co‐pyrolysis</topic><topic>Decomposition</topic><topic>Hydrocarbons</topic><topic>microalgae residue</topic><topic>oil sludge</topic><topic>Pyrolysis</topic><topic>Sludge</topic><topic>tube furnace</topic><topic>Tube furnaces</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Gong, Zhiqiang</creatorcontrib><creatorcontrib>Wang, Zhentong</creatorcontrib><creatorcontrib>Wang, Zhenbo</creatorcontrib><creatorcontrib>Du, Aixun</creatorcontrib><creatorcontrib>Fang, Peiwen</creatorcontrib><creatorcontrib>Sun, Zhiqian</creatorcontrib><creatorcontrib>Li, Xiaoyu</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Canadian journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Gong, Zhiqiang</au><au>Wang, Zhentong</au><au>Wang, Zhenbo</au><au>Du, Aixun</au><au>Fang, Peiwen</au><au>Sun, Zhiqian</au><au>Li, Xiaoyu</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Study on pyrolysis of oil sludge with microalgae residue additive</atitle><jtitle>Canadian journal of chemical engineering</jtitle><date>2018-09</date><risdate>2018</risdate><volume>96</volume><issue>9</issue><spage>1919</spage><epage>1925</epage><pages>1919-1925</pages><issn>0008-4034</issn><eissn>1939-019X</eissn><abstract>The pyrolysis of oil sludge (OS) with microalgae residue (MR) additive was conducted with a TGA and a tube furnace. The pyrolysis process of OS with the MR additive can be divided into three stages: 1) water evaporation, 2) the release of light groups of hydrocarbon compounds, the cracking of heavy groups, and carbon decomposition, and 3) minerals decomposition. With the MR addition ratio increasing, the yield of oil and gas increased, and oil to gas ratio increased during OS pyrolysis. The MR addition improved the quality of pyrolysis oil and gas from OS pyrolysis. The proportion of light oil increased from 38 % with a 5 % MR addition ratio to 45 % with a 30 % addition ratio. Major components of pyrolysis gas included H2, CO, CO2, and CxHy. With the increase of the MR blending ratio, CO and CO2 contents increased, while H2 and CxHy contents decreased. Adding MR favoured the transformation of heavy hydrocarbons (C6+), resulting in a high content of light hydrocarbons. This work can help promote massive synergistic treatment of OS and microalgae biomass.</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc</pub><doi>10.1002/cjce.23143</doi><tpages>7</tpages></addata></record> |
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source | Wiley Online Library - AutoHoldings Journals |
subjects | Algae Carbon dioxide Carbon monoxide co‐pyrolysis Decomposition Hydrocarbons microalgae residue oil sludge Pyrolysis Sludge tube furnace Tube furnaces |
title | Study on pyrolysis of oil sludge with microalgae residue additive |
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