Evaluation of the mass transfer effects on delignification kinetics of atmospheric acetic acid fractionation of sugarcane bagasse with a shrinking-layer model
[Display omitted] •Shrinking-layer model developed for acetic acid fractionation of biomass.•Mass transfer effects on the overall rate of delignification were evaluated.•Early stage was controlled by both internal diffusion and reaction.•Late stage was controlled by reaction. A shrinking-layer model...
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Veröffentlicht in: | Bioresource technology 2018-08, Vol.261, p.52-61 |
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creator | Zhao, Xuebing Wu, Ruchun Liu, Dehua |
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•Shrinking-layer model developed for acetic acid fractionation of biomass.•Mass transfer effects on the overall rate of delignification were evaluated.•Early stage was controlled by both internal diffusion and reaction.•Late stage was controlled by reaction.
A shrinking-layer model by modification of classical shrinking-core model was developed based on cell wall multi-layered structure for delignification of sugarcane bagasse with sulfuric acid (SA) catalyzed atmospheric acetic acid (AA) fractionation. The general model for overall rate of delignification was obtained and further employed to evaluate the mass transfer effects on delignification. It was found that the external diffusion could be neglected under the studied fractionation conditions, while the internal diffusion appeared to play an important role. The effective diffusion coefficient for lignin within the biomass was estimated as 6.7 × 10−14–1.6 × 10−12 m2/s depending on temperature, solid content in the system and molecular weight of lignin. However, surface reaction also seems to be a limiting step to the overall rate of delignification. At the early stage of delignification, both internal diffusion and reaction were controlling steps, while at the late stage reaction seems to be the controlling step. |
doi_str_mv | 10.1016/j.biortech.2018.03.140 |
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•Shrinking-layer model developed for acetic acid fractionation of biomass.•Mass transfer effects on the overall rate of delignification were evaluated.•Early stage was controlled by both internal diffusion and reaction.•Late stage was controlled by reaction.
A shrinking-layer model by modification of classical shrinking-core model was developed based on cell wall multi-layered structure for delignification of sugarcane bagasse with sulfuric acid (SA) catalyzed atmospheric acetic acid (AA) fractionation. The general model for overall rate of delignification was obtained and further employed to evaluate the mass transfer effects on delignification. It was found that the external diffusion could be neglected under the studied fractionation conditions, while the internal diffusion appeared to play an important role. The effective diffusion coefficient for lignin within the biomass was estimated as 6.7 × 10−14–1.6 × 10−12 m2/s depending on temperature, solid content in the system and molecular weight of lignin. However, surface reaction also seems to be a limiting step to the overall rate of delignification. At the early stage of delignification, both internal diffusion and reaction were controlling steps, while at the late stage reaction seems to be the controlling step.</description><identifier>ISSN: 0960-8524</identifier><identifier>EISSN: 1873-2976</identifier><identifier>DOI: 10.1016/j.biortech.2018.03.140</identifier><identifier>PMID: 29653334</identifier><language>eng</language><publisher>England: Elsevier Ltd</publisher><subject>Fractionation of lignocellulosic biomass ; Internal diffusion ; Kinetics ; Mass transfer ; Shrinking-layer model</subject><ispartof>Bioresource technology, 2018-08, Vol.261, p.52-61</ispartof><rights>2018 Elsevier Ltd</rights><rights>Copyright © 2018 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c405t-493f1a7e8ad4a55dbc528edf508105efa4be2c91cdf8f7b848bc0bf6be4348733</citedby><cites>FETCH-LOGICAL-c405t-493f1a7e8ad4a55dbc528edf508105efa4be2c91cdf8f7b848bc0bf6be4348733</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.biortech.2018.03.140$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/29653334$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Zhao, Xuebing</creatorcontrib><creatorcontrib>Wu, Ruchun</creatorcontrib><creatorcontrib>Liu, Dehua</creatorcontrib><title>Evaluation of the mass transfer effects on delignification kinetics of atmospheric acetic acid fractionation of sugarcane bagasse with a shrinking-layer model</title><title>Bioresource technology</title><addtitle>Bioresour Technol</addtitle><description>[Display omitted]
•Shrinking-layer model developed for acetic acid fractionation of biomass.•Mass transfer effects on the overall rate of delignification were evaluated.•Early stage was controlled by both internal diffusion and reaction.•Late stage was controlled by reaction.
A shrinking-layer model by modification of classical shrinking-core model was developed based on cell wall multi-layered structure for delignification of sugarcane bagasse with sulfuric acid (SA) catalyzed atmospheric acetic acid (AA) fractionation. The general model for overall rate of delignification was obtained and further employed to evaluate the mass transfer effects on delignification. It was found that the external diffusion could be neglected under the studied fractionation conditions, while the internal diffusion appeared to play an important role. The effective diffusion coefficient for lignin within the biomass was estimated as 6.7 × 10−14–1.6 × 10−12 m2/s depending on temperature, solid content in the system and molecular weight of lignin. However, surface reaction also seems to be a limiting step to the overall rate of delignification. At the early stage of delignification, both internal diffusion and reaction were controlling steps, while at the late stage reaction seems to be the controlling step.</description><subject>Fractionation of lignocellulosic biomass</subject><subject>Internal diffusion</subject><subject>Kinetics</subject><subject>Mass transfer</subject><subject>Shrinking-layer model</subject><issn>0960-8524</issn><issn>1873-2976</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNqFkctu1TAQhi0Eag-lr1B5ySapb0mcHagqbaVKbGBt-TI-8SGXg-0U9WV4VhydtltWI9nfzD_2h9AVJTUltL0-1CYsMYMdakaorAmvqSDv0I7Kjles79r3aEf6llSyYeIcfUzpQAjhtGNn6Jz1bcM5Fzv09_ZJj6vOYZnx4nEeAE86JZyjnpOHiMF7sDnhcu9gDPs5-GBP_K8wQw42bY06T0s6DhCDxdpux6UEh33UdoPfEtK619HqGbDR-5IE-E_IA9Y4DTHMZeS-GvVzCZ6WkvcJffB6THD5Ui_Qz2-3P27uq8fvdw83Xx8rK0iTK9FzT3UHUjuhm8YZ2zAJzjdEUtKA18IAsz21zkvfGSmkscT41oDgonwYv0CfT3OPcfm9QspqCsnCOJZFlzUpRljDGZUtLWh7Qm1cUorg1TGGScdnRYna3KiDenWjNjeKcFXclMarl4zVTODe2l5lFODLCYDy0qcAUSUbYLbgQiwOlFvC_zL-AU-vqII</recordid><startdate>20180801</startdate><enddate>20180801</enddate><creator>Zhao, Xuebing</creator><creator>Wu, Ruchun</creator><creator>Liu, Dehua</creator><general>Elsevier Ltd</general><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope></search><sort><creationdate>20180801</creationdate><title>Evaluation of the mass transfer effects on delignification kinetics of atmospheric acetic acid fractionation of sugarcane bagasse with a shrinking-layer model</title><author>Zhao, Xuebing ; Wu, Ruchun ; Liu, Dehua</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c405t-493f1a7e8ad4a55dbc528edf508105efa4be2c91cdf8f7b848bc0bf6be4348733</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Fractionation of lignocellulosic biomass</topic><topic>Internal diffusion</topic><topic>Kinetics</topic><topic>Mass transfer</topic><topic>Shrinking-layer model</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Zhao, Xuebing</creatorcontrib><creatorcontrib>Wu, Ruchun</creatorcontrib><creatorcontrib>Liu, Dehua</creatorcontrib><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><jtitle>Bioresource technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Zhao, Xuebing</au><au>Wu, Ruchun</au><au>Liu, Dehua</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Evaluation of the mass transfer effects on delignification kinetics of atmospheric acetic acid fractionation of sugarcane bagasse with a shrinking-layer model</atitle><jtitle>Bioresource technology</jtitle><addtitle>Bioresour Technol</addtitle><date>2018-08-01</date><risdate>2018</risdate><volume>261</volume><spage>52</spage><epage>61</epage><pages>52-61</pages><issn>0960-8524</issn><eissn>1873-2976</eissn><abstract>[Display omitted]
•Shrinking-layer model developed for acetic acid fractionation of biomass.•Mass transfer effects on the overall rate of delignification were evaluated.•Early stage was controlled by both internal diffusion and reaction.•Late stage was controlled by reaction.
A shrinking-layer model by modification of classical shrinking-core model was developed based on cell wall multi-layered structure for delignification of sugarcane bagasse with sulfuric acid (SA) catalyzed atmospheric acetic acid (AA) fractionation. The general model for overall rate of delignification was obtained and further employed to evaluate the mass transfer effects on delignification. It was found that the external diffusion could be neglected under the studied fractionation conditions, while the internal diffusion appeared to play an important role. The effective diffusion coefficient for lignin within the biomass was estimated as 6.7 × 10−14–1.6 × 10−12 m2/s depending on temperature, solid content in the system and molecular weight of lignin. However, surface reaction also seems to be a limiting step to the overall rate of delignification. At the early stage of delignification, both internal diffusion and reaction were controlling steps, while at the late stage reaction seems to be the controlling step.</abstract><cop>England</cop><pub>Elsevier Ltd</pub><pmid>29653334</pmid><doi>10.1016/j.biortech.2018.03.140</doi><tpages>10</tpages></addata></record> |
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subjects | Fractionation of lignocellulosic biomass Internal diffusion Kinetics Mass transfer Shrinking-layer model |
title | Evaluation of the mass transfer effects on delignification kinetics of atmospheric acetic acid fractionation of sugarcane bagasse with a shrinking-layer model |
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