Kinetic modeling of thermal decomposition of sugarcane bagasse in the inert gas environment
Sugarcane bagasse was characterized by thermogravimetric analysis (TGA) with the different heating rates, and nitrogen carrier from 30 to 800 oC. Through decreasing the sample's mass by temperature, the stage of thermal decomposition could be determined. Specifically, there were three stages of...
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Veröffentlicht in: | Vietnam journal of chemistry 2019-10, Vol.57 (5), p.574-580 |
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description | Sugarcane bagasse was characterized by thermogravimetric analysis (TGA) with the different heating rates, and nitrogen carrier from 30 to 800 oC. Through decreasing the sample's mass by temperature, the stage of thermal decomposition could be determined. Specifically, there were three stages of decomposition including moisture escape stage, decomposition of cellulose stage, hemicellulose and lignin decomposition stage. On the other hand, based on the results of TGA the activation energy of decomposition process was determined by the inverse of the Flynn‐Wall‐Ozawa (FWO) method and Kissinger‐Akahira‐Sunose (KAS) method. The calculated results were compared with the activation energy by the Coats‐Redfern method and Criado method in order to find the kinetics of bagasse pyrolysis process. Accordingly, when the conversion of reaction was lower than 75 %, corresponding to the decomposing process of hemicellulose and cellulose, the thermal decomposing process of bagasse obeyed diffusion kinetics of model D2, D3 and D4. |
doi_str_mv | 10.1002/vjch.201900077 |
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Through decreasing the sample's mass by temperature, the stage of thermal decomposition could be determined. Specifically, there were three stages of decomposition including moisture escape stage, decomposition of cellulose stage, hemicellulose and lignin decomposition stage. On the other hand, based on the results of TGA the activation energy of decomposition process was determined by the inverse of the Flynn‐Wall‐Ozawa (FWO) method and Kissinger‐Akahira‐Sunose (KAS) method. The calculated results were compared with the activation energy by the Coats‐Redfern method and Criado method in order to find the kinetics of bagasse pyrolysis process. Accordingly, when the conversion of reaction was lower than 75 %, corresponding to the decomposing process of hemicellulose and cellulose, the thermal decomposing process of bagasse obeyed diffusion kinetics of model D2, D3 and D4.</description><identifier>ISSN: 0866-7144</identifier><identifier>ISSN: 2572-8288</identifier><identifier>EISSN: 2572-8288</identifier><identifier>DOI: 10.1002/vjch.201900077</identifier><language>eng</language><publisher>Weinheim: WILEY‐VCH Verlag GmbH & Co. KGaA</publisher><subject>Kinetic model ; pyrolysis ; sugarcane bagasse ; thermal decomposition ; thermogravimetric analysis</subject><ispartof>Vietnam journal of chemistry, 2019-10, Vol.57 (5), p.574-580</ispartof><rights>2019 Vietnam Academy of Science and Technology, Hanoi & Wiley‐VCH Verlag GmbH & Co. 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Through decreasing the sample's mass by temperature, the stage of thermal decomposition could be determined. Specifically, there were three stages of decomposition including moisture escape stage, decomposition of cellulose stage, hemicellulose and lignin decomposition stage. On the other hand, based on the results of TGA the activation energy of decomposition process was determined by the inverse of the Flynn‐Wall‐Ozawa (FWO) method and Kissinger‐Akahira‐Sunose (KAS) method. The calculated results were compared with the activation energy by the Coats‐Redfern method and Criado method in order to find the kinetics of bagasse pyrolysis process. Accordingly, when the conversion of reaction was lower than 75 %, corresponding to the decomposing process of hemicellulose and cellulose, the thermal decomposing process of bagasse obeyed diffusion kinetics of model D2, D3 and D4.</description><subject>Kinetic model</subject><subject>pyrolysis</subject><subject>sugarcane bagasse</subject><subject>thermal decomposition</subject><subject>thermogravimetric analysis</subject><issn>0866-7144</issn><issn>2572-8288</issn><issn>2572-8288</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNqFkD1PwzAURS0EElXpyuw_kPLsfNgZUQUUqMRSsTBEjvOcukrsyg5F_fckKoKR6Ur3nfOGS8gtgyUD4HfHvd4tObASAIS4IDOeC55ILuUlmYEsikSwLLsmixj3I8JkkabAZuTj1TocrKa9b7CzrqXe0GGHoVcdbVD7_uCjHax30yF-tipo5ZDWqlUxIrVuosfAMNCxouiONnjXoxtuyJVRXcTFT87J9vFhu1onm7en59X9JtEpL0WSooQmEzxnkCtuCqaxMQYaoXLM6rpuskZggSbVCAIKzpnQXKJEMAC6TOdkeX6rg48xoKkOwfYqnCoG1TRONY1T_Y4zCuVZ-LIdnv6hq_eX1frP_QbbgWrE</recordid><startdate>201910</startdate><enddate>201910</enddate><creator>Van Nam, Huynh</creator><creator>Tam, Truong Thanh</creator><creator>Tho, Van Dinh Son</creator><general>WILEY‐VCH Verlag GmbH & Co. KGaA</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>201910</creationdate><title>Kinetic modeling of thermal decomposition of sugarcane bagasse in the inert gas environment</title><author>Van Nam, Huynh ; Tam, Truong Thanh ; Tho, Van Dinh Son</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3297-3e80d4725105a2f61cedff0d7a5e4bbbd4d7e6ef3ce07062217c28e8e0f00c93</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Kinetic model</topic><topic>pyrolysis</topic><topic>sugarcane bagasse</topic><topic>thermal decomposition</topic><topic>thermogravimetric analysis</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Van Nam, Huynh</creatorcontrib><creatorcontrib>Tam, Truong Thanh</creatorcontrib><creatorcontrib>Tho, Van Dinh Son</creatorcontrib><collection>CrossRef</collection><jtitle>Vietnam journal of chemistry</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Van Nam, Huynh</au><au>Tam, Truong Thanh</au><au>Tho, Van Dinh Son</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetic modeling of thermal decomposition of sugarcane bagasse in the inert gas environment</atitle><jtitle>Vietnam journal of chemistry</jtitle><date>2019-10</date><risdate>2019</risdate><volume>57</volume><issue>5</issue><spage>574</spage><epage>580</epage><pages>574-580</pages><issn>0866-7144</issn><issn>2572-8288</issn><eissn>2572-8288</eissn><abstract>Sugarcane bagasse was characterized by thermogravimetric analysis (TGA) with the different heating rates, and nitrogen carrier from 30 to 800 oC. Through decreasing the sample's mass by temperature, the stage of thermal decomposition could be determined. Specifically, there were three stages of decomposition including moisture escape stage, decomposition of cellulose stage, hemicellulose and lignin decomposition stage. On the other hand, based on the results of TGA the activation energy of decomposition process was determined by the inverse of the Flynn‐Wall‐Ozawa (FWO) method and Kissinger‐Akahira‐Sunose (KAS) method. The calculated results were compared with the activation energy by the Coats‐Redfern method and Criado method in order to find the kinetics of bagasse pyrolysis process. Accordingly, when the conversion of reaction was lower than 75 %, corresponding to the decomposing process of hemicellulose and cellulose, the thermal decomposing process of bagasse obeyed diffusion kinetics of model D2, D3 and D4.</abstract><cop>Weinheim</cop><pub>WILEY‐VCH Verlag GmbH & Co. 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subjects | Kinetic model pyrolysis sugarcane bagasse thermal decomposition thermogravimetric analysis |
title | Kinetic modeling of thermal decomposition of sugarcane bagasse in the inert gas environment |
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