Detailed gasification process of woody biomass-derived char with H2O and CO2 gasifying agents

IF 1.2 4区 工程技术 Q3 THERMODYNAMICS Journal of Thermal Science and Technology Pub Date : 2020-01-01 DOI:10.1299/jtst.2020jtst0035
Y. Okumura
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引用次数: 1

Abstract

Most gasification processes including updraft/downdraft gasifiers and entrained flow gasifiers involve partial combustion, wherein the combustion heat (approximately 800–1100 °C) is used. In the reduction zone of gasifiers, biomass pyrolysis and biochar gasification proceed in the presence of the H2O vapor and heat, and CO2 in the combustion area. (Thurner et al., 1981; Di-Blasi et al., 2001; Matsumoto et al., 2009; Guo et al., 2014; Ram et al., 2019.) Because the pyrolysis rate is much higher than the gasification rate of biochar, the overall conversion rate is controlled by the gasification rate of char. That is, the overall gasification rate is limited by the slow gasification rate of char. (Zhang et al., 2008; Okumura et al., 2009; Seo et al., 2010.) Many studies have been performed on the gasification of biochar. The gasification rate of biochar varies greatly with the experimental device and the type of biomass, even when the same gasification temperature is used. In addition, pore development in the biochar during gasification with H2O and CO2 agents, especially the relation between gasification reaction rate and interface area, has been rarely studied. The present study compared in detail the gasification rate of biochar in H2O gasifying agent with that in CO2 gasifying agent at 1073–1273 K using the same experimental apparatus and the same char samples, under the same pyrolysis conditions. The results showed that the gasification rate constant of the biochar was approximately 3–10 times higher under H2O compared to the CO2 gasifying agent. The specific surface area of woody biochar during H2O gasification was compared with that observed during CO2 gasification. When the overall gasification rates were almost same, the increase in the specific surface area of the pores under the H2O atmosphere was similar to that processed under the CO2 atmosphere i.e., no significant differences in pore development or physical shape were observed between the CO2 and H2O gasifying agents. * Faculty of Engineering and Design, Kagawa University Hayashi-cho, Takamatsu,761-0396, Japan E-mail: okumura.yukihiko@kagawa-u.ac.jp
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木质生物质炭用H2O和CO2气化剂气化的详细过程
大多数气化过程,包括上升气流/下降气流气化炉和夹带流气化炉涉及部分燃烧,其中燃烧热(约800-1100°C)被使用。在气化炉还原区,生物质热解和生物炭气化是在H2O蒸汽和热量存在的情况下进行的,而在燃烧区则有CO2存在。(Thurner et al., 1981;Di-Blasi et al., 2001;Matsumoto等人,2009;郭等,2014;Ram等人,2019。)由于热解速率远高于生物炭的气化速率,因此整体转化率受炭的气化速率控制。也就是说,整体气化速率受到焦炭气化速率缓慢的限制。(张等,2008;Okumura等人,2009;Seo et al., 2010)。人们对生物炭的气化进行了许多研究。即使在相同的气化温度下,生物炭的气化速率随实验装置和生物质类型的不同而变化很大。另外,对于生物炭在H2O和CO2作用下气化过程中的孔隙发育,特别是气化反应速率与界面面积之间的关系研究较少。本研究在1073 ~ 1273 K条件下,使用相同的实验设备、相同的炭样,详细比较了生物炭在H2O气化剂和CO2气化剂中的气化率。结果表明,生物炭在H2O条件下的气化速率常数约为CO2气化剂的3-10倍。将木质生物炭在H2O气化过程中的比表面积与CO2气化过程中的比表面积进行了比较。当总气化速率几乎相同时,H2O气氛下气孔比表面积的增加与CO2气氛下相似,即CO2和H2O两种气化剂在气孔发育和物理形态上没有显著差异。*香川大学工程与设计学院,高松,761-0396,日本E-mail: okumura.yukihiko@kagawa-u.ac.jp
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来源期刊
CiteScore
2.30
自引率
8.30%
发文量
0
审稿时长
5 months
期刊介绍: JTST covers a variety of fields in thermal engineering including heat and mass transfer, thermodynamics, combustion, bio-heat transfer, micro- and macro-scale transport phenomena and practical thermal problems in industrial applications.
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