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In-situ Upgrading of Napier Grass Pyrolysis Vapour Over Microporous and Hierarchical Mesoporous Zeolites
This study presents in-situ upgrading of pyrolysis vapour derived from Napier grass over microporous and mesoporous ZSM-5 catalysts. It evaluates effect of process variables such catalyst–biomass ratio and catalyst type in a vertical fixed bed pyrolysis system at 600 °C, 50 °C/min under 5 L/min nitr...
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Published in: | Waste and biomass valorization 2018-08, Vol.9 (8), p.1415-1428 |
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description | This study presents in-situ upgrading of pyrolysis vapour derived from Napier grass over microporous and mesoporous ZSM-5 catalysts. It evaluates effect of process variables such catalyst–biomass ratio and catalyst type in a vertical fixed bed pyrolysis system at 600 °C, 50 °C/min under 5 L/min nitrogen flow. Increasing catalyst–biomass ratio during the catalytic process with microporous structure reduced production of organic phase bio-oil by approximately 7.0 wt%. Using mesoporous catalyst promoted nearly 4.0 wt% higher organic yield relative to microporous catalyst, which translate to only about 3.0 wt% reduction in organic phase compared to the yield of organic phase from non-catalytic process. GC–MS analysis of bio-oil organic phase revealed maximum degree of deoxygenation of about 36.9% with microporous catalyst compared to the mesoporous catalysts, which had between 39 and 43%. Mesoporous catalysts promoted production olefins and alkanes, normal phenol, monoaromatic hydrocarbons while microporous catalyst favoured the production of alkenes and polyaromatic hydrocarbons. There was no significant increase in the production of normal phenols over microporous catalyst due to its inability to transform the methoxyphenols and methoxy aromatics. This study demonstrated that upgrading of Napier grass pyrolysis vapour over mesoporous ZSM-5 produced bio-oil with improved physicochemical properties. |
doi_str_mv | 10.1007/s12649-017-9925-x |
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There was no significant increase in the production of normal phenols over microporous catalyst due to its inability to transform the methoxyphenols and methoxy aromatics. 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It evaluates effect of process variables such catalyst–biomass ratio and catalyst type in a vertical fixed bed pyrolysis system at 600 °C, 50 °C/min under 5 L/min nitrogen flow. Increasing catalyst–biomass ratio during the catalytic process with microporous structure reduced production of organic phase bio-oil by approximately 7.0 wt%. Using mesoporous catalyst promoted nearly 4.0 wt% higher organic yield relative to microporous catalyst, which translate to only about 3.0 wt% reduction in organic phase compared to the yield of organic phase from non-catalytic process. GC–MS analysis of bio-oil organic phase revealed maximum degree of deoxygenation of about 36.9% with microporous catalyst compared to the mesoporous catalysts, which had between 39 and 43%. Mesoporous catalysts promoted production olefins and alkanes, normal phenol, monoaromatic hydrocarbons while microporous catalyst favoured the production of alkenes and polyaromatic hydrocarbons. There was no significant increase in the production of normal phenols over microporous catalyst due to its inability to transform the methoxyphenols and methoxy aromatics. This study demonstrated that upgrading of Napier grass pyrolysis vapour over mesoporous ZSM-5 produced bio-oil with improved physicochemical properties.</description><subject>Alkanes</subject><subject>Alkenes</subject><subject>Aromatic compounds</subject><subject>Biomass</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Deoxygenation</subject><subject>Engineering</subject><subject>Environment</subject><subject>Environmental Engineering/Biotechnology</subject><subject>Fixed beds</subject><subject>Grasses</subject><subject>Hydrocarbons</subject><subject>Industrial Pollution Prevention</subject><subject>Oil</subject><subject>Original Paper</subject><subject>Phenols</subject><subject>Physicochemical properties</subject><subject>Polycyclic aromatic hydrocarbons</subject><subject>Process variables</subject><subject>Pyrolysis</subject><subject>Renewable and Green Energy</subject><subject>Solvents</subject><subject>Upgrading</subject><subject>Vapors</subject><subject>Waste Management/Waste Technology</subject><subject>Zeolites</subject><issn>1877-2641</issn><issn>1877-265X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp1kE1LAzEQhoMoWGp_gLeA52g-usnuUYq2hVY9WBEvIZtN2pR1syZdaf-9KevHydMMzPu-M_MAcEnwNcFY3ERC-bhAmAhUFDRD-xMwILkQiPLs9fS3H5NzMIpxizGmhOSUiQHYzBsU3a6Dq3YdVOWaNfQWPqjWmQCnQcUInw7B14foInxRre8CfPxMs6XTwbc--C5C1VRwlgwq6I3TqoZLE39mb8bXbmfiBTizqo5m9F2HYHV_9zyZocXjdD65XSDNMrZD3JqqLKnloiAZt3mRC6VtxZnAY81YhRXVSqhSFLrUVWlzYbnmlShJVnCaFENw1ee2wX90Ju7kNt3cpJWSYs4YybNcJBXpVemJGIOxsg3uXYWDJFgemcqeqUxM5ZGp3CcP7T0xaZu1CX_J_5u-AJyXfEw</recordid><startdate>20180801</startdate><enddate>20180801</enddate><creator>Mohammed, Isah Yakub</creator><creator>Abakr, Yousif Abdalla</creator><creator>Kazi, Feroz Kabir</creator><general>Springer Netherlands</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20180801</creationdate><title>In-situ Upgrading of Napier Grass Pyrolysis Vapour Over Microporous and Hierarchical Mesoporous Zeolites</title><author>Mohammed, Isah Yakub ; Abakr, Yousif Abdalla ; Kazi, Feroz Kabir</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c353t-6fedbb2f679156f8987acfd63704c33d0a2ca7ab79cbcdbf87f6c6d7b15962c33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Alkanes</topic><topic>Alkenes</topic><topic>Aromatic compounds</topic><topic>Biomass</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Deoxygenation</topic><topic>Engineering</topic><topic>Environment</topic><topic>Environmental Engineering/Biotechnology</topic><topic>Fixed beds</topic><topic>Grasses</topic><topic>Hydrocarbons</topic><topic>Industrial Pollution Prevention</topic><topic>Oil</topic><topic>Original Paper</topic><topic>Phenols</topic><topic>Physicochemical properties</topic><topic>Polycyclic aromatic hydrocarbons</topic><topic>Process variables</topic><topic>Pyrolysis</topic><topic>Renewable and Green Energy</topic><topic>Solvents</topic><topic>Upgrading</topic><topic>Vapors</topic><topic>Waste Management/Waste Technology</topic><topic>Zeolites</topic><toplevel>online_resources</toplevel><creatorcontrib>Mohammed, Isah Yakub</creatorcontrib><creatorcontrib>Abakr, Yousif Abdalla</creatorcontrib><creatorcontrib>Kazi, Feroz Kabir</creatorcontrib><collection>CrossRef</collection><jtitle>Waste and biomass valorization</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mohammed, Isah Yakub</au><au>Abakr, Yousif Abdalla</au><au>Kazi, Feroz Kabir</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>In-situ Upgrading of Napier Grass Pyrolysis Vapour Over Microporous and Hierarchical Mesoporous Zeolites</atitle><jtitle>Waste and biomass valorization</jtitle><stitle>Waste Biomass Valor</stitle><date>2018-08-01</date><risdate>2018</risdate><volume>9</volume><issue>8</issue><spage>1415</spage><epage>1428</epage><pages>1415-1428</pages><issn>1877-2641</issn><eissn>1877-265X</eissn><abstract>This study presents in-situ upgrading of pyrolysis vapour derived from Napier grass over microporous and mesoporous ZSM-5 catalysts. It evaluates effect of process variables such catalyst–biomass ratio and catalyst type in a vertical fixed bed pyrolysis system at 600 °C, 50 °C/min under 5 L/min nitrogen flow. Increasing catalyst–biomass ratio during the catalytic process with microporous structure reduced production of organic phase bio-oil by approximately 7.0 wt%. Using mesoporous catalyst promoted nearly 4.0 wt% higher organic yield relative to microporous catalyst, which translate to only about 3.0 wt% reduction in organic phase compared to the yield of organic phase from non-catalytic process. GC–MS analysis of bio-oil organic phase revealed maximum degree of deoxygenation of about 36.9% with microporous catalyst compared to the mesoporous catalysts, which had between 39 and 43%. Mesoporous catalysts promoted production olefins and alkanes, normal phenol, monoaromatic hydrocarbons while microporous catalyst favoured the production of alkenes and polyaromatic hydrocarbons. There was no significant increase in the production of normal phenols over microporous catalyst due to its inability to transform the methoxyphenols and methoxy aromatics. This study demonstrated that upgrading of Napier grass pyrolysis vapour over mesoporous ZSM-5 produced bio-oil with improved physicochemical properties.</abstract><cop>Dordrecht</cop><pub>Springer Netherlands</pub><doi>10.1007/s12649-017-9925-x</doi><tpages>14</tpages></addata></record> |
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subjects | Alkanes Alkenes Aromatic compounds Biomass Catalysis Catalysts Deoxygenation Engineering Environment Environmental Engineering/Biotechnology Fixed beds Grasses Hydrocarbons Industrial Pollution Prevention Oil Original Paper Phenols Physicochemical properties Polycyclic aromatic hydrocarbons Process variables Pyrolysis Renewable and Green Energy Solvents Upgrading Vapors Waste Management/Waste Technology Zeolites |
title | In-situ Upgrading of Napier Grass Pyrolysis Vapour Over Microporous and Hierarchical Mesoporous Zeolites |
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