Co-Gasification of Pistachio Shells with Wood Pellets in a Semi-Industrial Hybrid Cross/Updraft Reactor for Producer Gas and Biochar Production

Fire Pub Date : 2024-03-14 DOI:10.3390/fire7030087
Jiří Ryšavý, Jakub Čespiva, L. Kuboňová, Milan Dej, Katarzyna Szramowiat-Sala, Oleksandr Molchanov, Lukasz Niedzwiecki, Wei-Mon Yan, S. Thangavel
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Abstract

The possibilities of pistachio shell biochar production on laboratory-scale gasification and pyrolysis devices have been described by several previous studies. Nevertheless, the broader results of the pistachio shell co-gasification process on pilot-scale units have not yet been properly investigated or reported, especially regarding the detailed description of the biochar acquired during the routine operation. The biochar was analysed using several analytical techniques, such as ultimate and proximate analysis (62%wt of C), acid–base properties analysis (pH 9.52), Fourier-transform infrared spectroscopy (the presence of –OH bonds and identification of cellulose, hemicellulose and lignin), Raman spectroscopy (no determination of Id/Ig ratio due to high fluorescence), and nitrogen physisorption (specific surface 50.895 m2·g−1). X-ray fluorescence analysis exhibited the composition of the main compounds in the biochar ash (32.5%wt of Cl and 40.02%wt of Na2O). From the energy generation point of view, the lower heating value of the producer gas achieved 6.53 MJ·m−3 during the co-gasification. The relatively high lower heating value of the producer gas was mainly due to the significant volume fractions of CO (6.5%vol.), CH4 (14.2%vol.), and H2 (4.8 %vol.), while hot gas efficiency accomplished 89.6%.
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在半工业混合交叉/上气流反应器中对开心果壳和木质颗粒进行联合气化,以生产煤气和生物炭
之前的一些研究已经描述了在实验室规模的气化和热解装置上生产开心果壳生物炭的可能性。然而,对试点规模装置上开心果壳共气化过程的更广泛结果尚未进行适当的调查或报告,特别是对常规操作过程中获得的生物炭的详细描述。对生物炭的分析采用了多种分析技术,如最终和近似分析(62% 重量的 C)、酸碱特性分析(pH 值 9.52)、傅立叶变换红外光谱(存在 -OH 键和纤维素、半纤维素和木质素的鉴定)、拉曼光谱(由于高荧光而无法确定 Id/Ig 比率)和氮物理吸附(比表面 50.895 m2-g-1)。X 射线荧光分析显示了生物炭灰中主要化合物的组成(32.5% 重量的 Cl 和 40.02% 重量的 Na2O)。从能源生产的角度来看,在联合气化过程中,生产气体的较低热值达到了 6.53 MJ-m-3。生产气热值相对较低的主要原因是 CO(6.5%体积分数)、CH4(14.2%体积分数)和 H2(4.8%体积分数)的体积分数较大,而热气效率达到 89.6%。
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