Experimental study and characterisation of a novel two stage bubbling fluidised bed gasification process utilising municipal waste wood

IF 7.2 2区 工程技术 Q1 CHEMISTRY, APPLIED
M. Kresta , D. Gurtner , L. Nohel , A. Hofmann , C. Pfeifer
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Abstract

Biomass gasification has increased due to its ability to provide high-temperature heat, making it promising for the decarbonisation of industrial processes. The economic and technical challenges of large-scale operations need to be addressed by focusing on small-sized gasifiers, while the use of low-grade biomass, is essential to increase the flexibility and sustainability of the plant. However, the utilisation of low-grade biomass is hindered by challenges stemming from variations in the particle distribution and shape, which significantly impact the fluidisation process and overall. In this research, the gasification of shredded municipal waste wood in a pilot-scale bubbling fluidised bed reactor was demonstrated, and the fluid-dynamics and gas production were assessed. The gasification process was yielding a gas with a lower heating value between 3.5 MJNm−3 and 3.9 MJNm−3 and a cold gas efficiency (CGE) of 46.4 %–48.6 %. Notably, these CGE values are consistent with pilot-scale setups, where CGE values above 50 % are typically not achievable because of poor insulation standards. The reactor's conical shape facilitated dynamic fluid regime transitions, ensuring efficient gas-solid interactions. This design allowed optimisation of fluidisation by accommodating particles of varying sizes throughout the reactor's height, thereby promoting efficient gasification suitable for industrial applications with diverse biomass feedstocks.
利用城市废木料的新型两级鼓泡流化床气化工艺的实验研究和特性分析
生物质气化因其提供高温热量的能力而得到越来越多的关注,使其在工业过程的脱碳方面大有可为。大规模运营所面临的经济和技术挑战需要通过关注小型气化炉来解决,而使用低品位生物质对于提高工厂的灵活性和可持续性至关重要。然而,低品位生物质的利用受到颗粒分布和形状变化带来的挑战的阻碍,这对流化过程和整体产生了重大影响。在这项研究中,我们演示了在中试规模的鼓泡流化床反应器中气化城市废木屑的过程,并对流体动力学和气体产量进行了评估。气化过程产生的气体热值较低,介于 3.5 MJNm-3 和 3.9 MJNm-3 之间,冷气效率 (CGE) 为 46.4 %-48.6 %。值得注意的是,这些 CGE 值与中试规模的装置一致,在中试规模装置中,由于隔热标准较差,CGE 值通常无法达到 50 % 以上。反应器的圆锥形有利于流体的动态转换,确保了有效的气固相互作用。这种设计通过在反应器的整个高度上容纳不同大小的颗粒来优化流化,从而促进了高效气化,适用于各种生物质原料的工业应用。
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来源期刊
Fuel Processing Technology
Fuel Processing Technology 工程技术-工程:化工
CiteScore
13.20
自引率
9.30%
发文量
398
审稿时长
26 days
期刊介绍: Fuel Processing Technology (FPT) deals with the scientific and technological aspects of converting fossil and renewable resources to clean fuels, value-added chemicals, fuel-related advanced carbon materials and by-products. In addition to the traditional non-nuclear fossil fuels, biomass and wastes, papers on the integration of renewables such as solar and wind energy and energy storage into the fuel processing processes, as well as papers on the production and conversion of non-carbon-containing fuels such as hydrogen and ammonia, are also welcome. While chemical conversion is emphasized, papers on advanced physical conversion processes are also considered for publication in FPT. Papers on the fundamental aspects of fuel structure and properties will also be considered.
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