木质生物质的氧化焙烧:引入修正的严重程度系数

IF 3.5 4区 工程技术 Q3 ENERGY & FUELS
Udya Madhavi Aravindi Devaraja, Chamini Lakshika Wickramarathna Dissanayake, Duleeka Sandamali Gunarathne, Wei-Hsin Chen
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引用次数: 0

摘要

在 3-9% 的氧气环境中,在 250-300 °C 的温度下对橡胶木和胶合木进行了 30-60 分钟的热解实验,以研究其氧化热解行为。在最苛刻的氧化条件下,橡胶木的较高热值从 18.9 兆焦/千克增加到 24.68 兆焦/千克,糯米糍的较高热值从 19.46 兆焦/千克增加到 23.19 兆焦/千克。采用响应面方法模拟了热解条件对固体产量、VM 去除率、C 提高率、HHV 提高率和能量产量的影响,温度和氧气浓度是影响热解生物质特性的主要因素。橡胶木的能量质量共同效益指数(EMCI)明显高于胶合木。糯米茄氧化热解的 EMCI 与惰性条件下的 EMCI 没有明显差异。为氧化干烧引入了一个新的严重性因子,归一化的严重性因子与干烧生物质的特性呈线性相关,这有助于氧化干烧模型的建立。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Oxidative torrefaction of woody biomass: introducing a modified severity factor

Oxidative torrefaction of woody biomass: introducing a modified severity factor

Torrefaction experiments of Rubberwood and Gliricidia were conducted at 250–300 °C for 30–60 min in a 3–9% oxygen environment to study the oxidative torrefaction behavior. The higher heating value of the torrefied Rubberwood increased from 18.9 to 24.68 MJ/kg and from 19.46 to 23.19 MJ/kg for Gliricidia under the most severe oxidative conditions. Effects of torrefaction conditions on the solid yield, VM removal, C enhancement, HHV enhancement, and energy yield were modeled using response surface methodology, and temperature and oxygen concentration mainly affected the torrefied biomass properties. Rubberwood recorded a significantly greater energy mass co-benefit index (EMCI) than Gliricidia. EMCI of oxidative torrefaction of Gliricidia showed no significant difference from that of inert conditions. A new severity factor was introduced for oxidative torrefaction, and the normalized severity factor showed a linear correlation with torrefied biomass properties, which could facilitate oxidative torrefaction modeling.

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来源期刊
Biomass Conversion and Biorefinery
Biomass Conversion and Biorefinery Energy-Renewable Energy, Sustainability and the Environment
CiteScore
7.00
自引率
15.00%
发文量
1358
期刊介绍: Biomass Conversion and Biorefinery presents articles and information on research, development and applications in thermo-chemical conversion; physico-chemical conversion and bio-chemical conversion, including all necessary steps for the provision and preparation of the biomass as well as all possible downstream processing steps for the environmentally sound and economically viable provision of energy and chemical products.
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