Process optimization and economic evaluation of air gasification of Saudi Arabian date palm fronds for H2-rich syngas using response surface methodology
[Display omitted] •Saudi Arabian date palm fronds (DPF) were used as feedstock in air gasification.•RSM was used to optimize, gasification process for high H2 and low CO2 in syngas.•Higher gasification temperature favours the production of H2 and CO yield in syngas.•CO2 formation suppresses at a hig...
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Veröffentlicht in: | Fuel (Guildford) 2022-05, Vol.316, p.123359, Article 123359 |
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Sprache: | eng |
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•Saudi Arabian date palm fronds (DPF) were used as feedstock in air gasification.•RSM was used to optimize, gasification process for high H2 and low CO2 in syngas.•Higher gasification temperature favours the production of H2 and CO yield in syngas.•CO2 formation suppresses at a higher gasification temperature.•Production cost of syngas obtained from DPF gasification was found as SAR 4.04/kg.
The transition of energy extraction from the fossil fuel to renewable energy is a primary drive-in world. Saudi Arabia is one of the big producer of date fruit which generates an abundant amount of date palm wastes. There is no proper utilization of these wastes in Saudi Arabia. Conversion of date palm waste into energy is a major potential alternative source of bioenergy via gasification. In current study, process optimization and economic evaluation of air gasification of date palm fronds (DPF) has been performed in downdraft gasifier for energy conversion. The impact of three process parameters temperature, air flowrate, and feedstock particle size on gas composition were investigated. The response surface methodology (RSM) was adopted for experimental design, optimization, and individual and interactive effects of parameters on H2 and CO compositions to find their optimum values. Temperature is the most influencing factor for H2 composition and it varies from 6 vol% to 18 vol% which is higher compared to air flowrate and feedstock particle size. A similar pattern of influencing factors was observed for CO composition it varies from 8 vol% to 20 vol%. The enrichment of H2and CO is due to the activation of endothermic reactions at elevated temperature. On the other hand, factor influencing order for CO2composition as feedstock particle size > air flowrate > temperature. The optimum conditions were found 900℃ temperature, 1 l/min air flowrate, and 6 mm feedstock particle size to maximizing the H2 and CO compositions. Cost of syngas produced from air gasification of DPF was determined SAR 4.04/kg which can be minimized to scale-up the gasification system. DPF conversion into energy is environmentally friendly alternative source of renewable energy that will helps to reduce the dependency on fossil fuel. |
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ISSN: | 0016-2361 1873-7153 |
DOI: | 10.1016/j.fuel.2022.123359 |