Experimental investigation and optimization of the gasification parameters of macadamia nutshells in a batch-fed bubbling fluidized bed gasifier with air preheating

Fredrick Irungu Njuguna , Hiram M. Ndiritu , Benson B. Gathitu , Meshack Hawi , Jotham Muthoka Munyalo
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引用次数: 2

Abstract

Gasification of biomass waste has a significant potential to reduce environmental impact and promote sustainability by producing syngas, which is considered as renewable energy. This work investigated the gasification of macadamia nutshells in air-preheated, batch-fed fluidized bed gasifier. The study conducted a parametric analysis to assess the effect of equivalence ratio (ER) and air temperature on the gasifier temperature profile and its performance based on gas composition, higher heating value (HHV), and gas yield. The research was conducted within the range of 0.15–0.35 for the equivalence ratio and 25–825 °C for the air temperature. Multi-objective numerical optimization was conducted using response surface methodology (RSM). From the parametric study, a distinct temperature profile was observed along the gasifier height, with the peak temperature near the top of the fluidized bed section and the lowest temperature at the top of the gasifier. Air preheating mostly favored gasification temperature at the lower part of the gasifier and showed rare significance at the top. No improvement in gasifier performance was observed beyond an air temperature of 620 °C, which was identified as the ideal air-preheating temperature. Analysis of variance (ANOVA) revealed that the equivalence ratio was the most influential parameter in the production of combustible gasses, syngas HHV and gas yield. Air preheating did not have a significant effect on methane production and gas yield. The most optimal values for ER and air temperature were obtained as 0.195 °C and 620 °C, respectively, producing optimal values of 9.54, 14.65%, 2.03, 4.02 MJ· Nm−3, and 1.82 Nm3· kg−1 for hydrogen, carbon monoxide, methane, HHV, and gas yield, respectively.

带空气预热的间歇进料鼓泡流化床气化炉中澳洲坚果壳气化参数的实验研究与优化
生物质废物气化产生的合成气被认为是可再生能源,在减少环境影响和促进可持续发展方面具有巨大潜力。这项研究调查了澳洲坚果壳在空气预热、批量进料流化床气化炉中的气化过程。该研究进行了参数分析,以评估等效比(ER)和空气温度对气化炉温度曲线的影响,以及基于气体成分、较高热值(HHV)和气体产量的气化炉性能。研究在当量比为 0.15-0.35 和空气温度为 25-825 °C 的范围内进行。采用响应面法(RSM)进行了多目标数值优化。从参数研究中可以看出,沿气化炉高度方向有明显的温度分布,流化床部分顶部附近温度最高,气化炉顶部温度最低。空气预热主要有利于气化炉下部的气化温度,而在气化炉顶部则很少有意义。空气温度超过 620 °C 时,气化器性能没有改善,该温度被认为是理想的空气预热温度。方差分析(ANOVA)显示,当量比是对可燃气体产量、合成气 HHV 和产气量影响最大的参数。空气预热对甲烷产量和气体产量的影响不大。ER 和空气温度的最佳值分别为 0.195 °C 和 620 °C,氢气、一氧化碳、甲烷、HHV 和气体产量的最佳值分别为 9.54%、14.65%、2.03、4.02 MJ- Nm-3 和 1.82 Nm3- kg-1。
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