Zepeng Cheng , Zhiwen Chen , Mingfeng Wang , Yongzhi Ren , Ke Zhang
{"title":"桉木屑热解动力学分析与数值模拟","authors":"Zepeng Cheng , Zhiwen Chen , Mingfeng Wang , Yongzhi Ren , Ke Zhang","doi":"10.1016/j.indcrop.2025.122045","DOIUrl":null,"url":null,"abstract":"<div><div>In this study, thermogravimetric analysis (TGA) was employed to investigate the thermal decomposition characteristics and kinetic parameters of eucalyptus sawdust at heating rates of 5, 10, 15, 20, and 30 ℃/min (20–900℃) under a nitrogen atmosphere (99.99 %, 30 mL/min). The pyrolysis process of eucalyptus sawdust was divided into three stages: drying and preheating (DH), fast weight-losing pyrolysis (FP) and carbon growing (CG). Mechanism function fitting determined that the DH and FP stages followed follow n-order reaction and Jander-type 3D diffusion, respectively. The activation energy (<em>E</em>), pre-exponential factor logarithm (lg<em>A</em>) and reaction order (<em>n</em>) of the DH and FP stages are 82.42 and 143.40 kJ/mol, 10.77 and 9.00 s<sup>−1</sup>, and 2.58 and 2.00, respectively. The results are highly consistent with the <em>E</em> and lg<em>A</em> values estimated by FWO and Friedman methods in the conversion rate (<em>α</em>) range of 0.2–0.8. For the CG stage, a new reaction process fitting equation (<span><math><mrow><mi>α</mi><mo>=</mo><mn>0.8695</mn><msup><mrow><mi>β</mi></mrow><mrow><mn>0.1319</mn></mrow></msup><mspace></mspace><mi>ln</mi><mspace></mspace><mi>T</mi><mo>−</mo><mn>5.0275</mn><msup><mrow><mi>β</mi></mrow><mrow><mn>0.1442</mn></mrow></msup></mrow></math></span>) was developed by numerical simulation of fitting <em>α</em>, temperature (<em>T</em>) and heating rate <em>(β</em>). The high coefficient of determination (R<sup>2</sup>>0.9700) confirms the equation's reliability. This study provides crucial theoretical support for optimizing the pyrolysis process of eucalyptus sawdust and guiding the reactor design.</div></div>","PeriodicalId":13581,"journal":{"name":"Industrial Crops and Products","volume":"236 ","pages":"Article 122045"},"PeriodicalIF":6.2000,"publicationDate":"2025-10-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Kinetics analysis and numerical simulation of eucalyptus sawdust pyrolysis\",\"authors\":\"Zepeng Cheng , Zhiwen Chen , Mingfeng Wang , Yongzhi Ren , Ke Zhang\",\"doi\":\"10.1016/j.indcrop.2025.122045\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>In this study, thermogravimetric analysis (TGA) was employed to investigate the thermal decomposition characteristics and kinetic parameters of eucalyptus sawdust at heating rates of 5, 10, 15, 20, and 30 ℃/min (20–900℃) under a nitrogen atmosphere (99.99 %, 30 mL/min). The pyrolysis process of eucalyptus sawdust was divided into three stages: drying and preheating (DH), fast weight-losing pyrolysis (FP) and carbon growing (CG). Mechanism function fitting determined that the DH and FP stages followed follow n-order reaction and Jander-type 3D diffusion, respectively. The activation energy (<em>E</em>), pre-exponential factor logarithm (lg<em>A</em>) and reaction order (<em>n</em>) of the DH and FP stages are 82.42 and 143.40 kJ/mol, 10.77 and 9.00 s<sup>−1</sup>, and 2.58 and 2.00, respectively. The results are highly consistent with the <em>E</em> and lg<em>A</em> values estimated by FWO and Friedman methods in the conversion rate (<em>α</em>) range of 0.2–0.8. For the CG stage, a new reaction process fitting equation (<span><math><mrow><mi>α</mi><mo>=</mo><mn>0.8695</mn><msup><mrow><mi>β</mi></mrow><mrow><mn>0.1319</mn></mrow></msup><mspace></mspace><mi>ln</mi><mspace></mspace><mi>T</mi><mo>−</mo><mn>5.0275</mn><msup><mrow><mi>β</mi></mrow><mrow><mn>0.1442</mn></mrow></msup></mrow></math></span>) was developed by numerical simulation of fitting <em>α</em>, temperature (<em>T</em>) and heating rate <em>(β</em>). The high coefficient of determination (R<sup>2</sup>>0.9700) confirms the equation's reliability. This study provides crucial theoretical support for optimizing the pyrolysis process of eucalyptus sawdust and guiding the reactor design.</div></div>\",\"PeriodicalId\":13581,\"journal\":{\"name\":\"Industrial Crops and Products\",\"volume\":\"236 \",\"pages\":\"Article 122045\"},\"PeriodicalIF\":6.2000,\"publicationDate\":\"2025-10-08\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Industrial Crops and Products\",\"FirstCategoryId\":\"97\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0926669025015912\",\"RegionNum\":1,\"RegionCategory\":\"农林科学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"AGRICULTURAL ENGINEERING\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial Crops and Products","FirstCategoryId":"97","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0926669025015912","RegionNum":1,"RegionCategory":"农林科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"AGRICULTURAL ENGINEERING","Score":null,"Total":0}
Kinetics analysis and numerical simulation of eucalyptus sawdust pyrolysis
In this study, thermogravimetric analysis (TGA) was employed to investigate the thermal decomposition characteristics and kinetic parameters of eucalyptus sawdust at heating rates of 5, 10, 15, 20, and 30 ℃/min (20–900℃) under a nitrogen atmosphere (99.99 %, 30 mL/min). The pyrolysis process of eucalyptus sawdust was divided into three stages: drying and preheating (DH), fast weight-losing pyrolysis (FP) and carbon growing (CG). Mechanism function fitting determined that the DH and FP stages followed follow n-order reaction and Jander-type 3D diffusion, respectively. The activation energy (E), pre-exponential factor logarithm (lgA) and reaction order (n) of the DH and FP stages are 82.42 and 143.40 kJ/mol, 10.77 and 9.00 s−1, and 2.58 and 2.00, respectively. The results are highly consistent with the E and lgA values estimated by FWO and Friedman methods in the conversion rate (α) range of 0.2–0.8. For the CG stage, a new reaction process fitting equation () was developed by numerical simulation of fitting α, temperature (T) and heating rate (β). The high coefficient of determination (R2>0.9700) confirms the equation's reliability. This study provides crucial theoretical support for optimizing the pyrolysis process of eucalyptus sawdust and guiding the reactor design.
期刊介绍:
Industrial Crops and Products is an International Journal publishing academic and industrial research on industrial (defined as non-food/non-feed) crops and products. Papers concern both crop-oriented and bio-based materials from crops-oriented research, and should be of interest to an international audience, hypothesis driven, and where comparisons are made statistics performed.