典型预处理条件下甘蔗渣伪组分热分解动力学研究:建立可行的初级生物精制的机会模拟

Juliana Otavia Bahú , Roger Assis de Oliveira , Leticia Mayuri Aiacyda De Souza , Elmer Ccopa Rivera , Romilda Fernandez Felisbino , Rubens Maciel Filho , Laura Plazas Tovar
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引用次数: 1

摘要

深入了解甘蔗渣(SCB)热降解的动力学和热力学参数,对于确定可再生燃料生产中初级生物精炼的适当条件至关重要。本文采用热重法研究了SCB高聚物的热降解动力学。采用无模型法和模型拟合法计算表观活化能(Ea)及其他相关反应参数。这项工作的一个重要进展是通过扩散控制反应和有序模型控制的多阶段模型对降解过程(一个吸热和非自发过程)进行定量解释,这有助于解释在生物精炼过程中观察到的质量平衡差异。根据衍生热重曲线,有三个主要峰与伪组分(PSE)相关:PSE 1(半纤维素+提取物和木质素)、PSE 2(纤维素+提取物和木质素)和PSE 3(木质素+提取物和残留的全麦纤维素)。对于PSE 1、PSE 2和PSE 3,采用Kissinger-Akahira-Sunose法分别得到124 ~ 154、147 ~ 153和230 ~ 530 kJ⋅mol - 1,采用Flynn-Wall-Ozawa法分别得到120 ~ 152、144 ~ 150和232 ~ 545 kJ⋅mol - 1。这些数据支持生物炼制过程中许多关键操作参数的计算,如最低预处理温度。SCB生物精炼在473.15 K下持续200分钟,可导致PSE 1、PSE 2和PSE 3的降解率分别高达10%、0.5%和11%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

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Kinetic study of thermal decomposition of sugarcane bagasse pseudo-components at typical pretreatment conditions: Simulations of opportunities towards the establishment of a feasible primary biorefining

A deeper understanding of the kinetic and thermodynamic parameters of thermal degradation of sugarcane bagasse (SCB) is fundamental to defining appropriate conditions for primary biorefining in the production of renewable fuels. In this work, the kinetics of thermal degradation of high polymers of SCB was investigated through thermogravimetric data. Model-free and model-fitting methods were used to calculate apparent activation energies (Ea) and other related reaction parameters. An essential advance of this work is related to the quantitative interpretation of the degradation process (an endothermic and non-spontaneous process) via a multi-stage model governed by diffusion-controlled reactions and order-based models, which helps explain the differences observed in the mass balance of biorefining processes. Based on derivative thermogravimetric curves, three major peaks were associated with pseudo-components (PSE): PSE 1 (hemicelluloses + extractives and lignin), PSE 2 (cellulose + extractives and lignin), and PSE 3 (lignin + extractives and residual holocellulose). For PSE 1, PSE 2, and PSE 3, respectively, Ea ranges of 124–154, 147–153, and 230–530 kJ⋅mol−1 were obtained using the Kissinger-Akahira-Sunose method, and 120–152, 144–150, and 232–545 kJ⋅mol−1 were obtained using the Flynn-Wall-Ozawa method. These data support the calculation of many critical operating parameters of biorefinery processes, such as the minimum pretreatment temperature. SCB biorefining could lead to a degradation of up to 10, 0.5, and 11% of PSE 1, PSE 2, and PSE 3, respectively, at 473.15 K for 200 min.

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