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Hydrogen and syngas yield from residual branches of oil palm tree using steam gasification

机译:利用蒸汽气化从油棕树的残留分支中产生氢气和合成气

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Wastes produced during oil palm production from agro-industries have great potential as a source of renewable energy in agriculturally rich countries, such as Thailand and Malaysia. Clean chemical energy recovery from oil palm residual branches via steam gasification is investigated here. A semi-batch reactor was used to investigate the gasification of palm trunk wastes at different reactor temperatures in the range of 600 to 1000 ℃. The steam flow rate was fixed at 3.10 g/min. Characteristics and overall yield of syngas properties are presented and discussed. Results show that gasification temperature slightly affects the overall syngas yield. However, the chemical composition of the syngas varied tremendously with the reactor temperature. Consequently, the syngas heating value and ratio of energy yield to energy consumed were found to be strongly dependent on the reactor temperature. Both the heating value and energy yield ratio increased with increase in reactor temperature. Gasification duration and the steam to solid fuel ratio indicate that reaction rate becomes progressively slower at reactor temperatures of less than 700 ℃. The results reveal that steam gasification of oil palm residues should not be carried out at reactor temperatures lower than 700 ℃, since a large amount of steam is consumed per unit mass of the sample in order to gasify the residual char.
机译:在泰国和马来西亚等农业富裕的国家中,从农业工业生产油棕的过程中产生的废物具有巨大的潜力,可作为可再生能源的来源。本文研究了通过蒸汽气化从油棕残留物分支中回收清洁化学能的方法。使用半间歇式反应器研究了在600到1000℃范围内不同反应器温度下棕榈树干废物的气化。蒸汽流速固定为3.10 g / min。介绍并讨论了合成气特性的特性和总收率。结果表明,气化温度对总合成气收率有轻微影响。但是,合成气的化学组成随反应器温度而变化很大。因此,发现合成气的热值以及能量产率与消耗能量的比率在很大程度上取决于反应器温度。热值和能量产率比均随着反应器温度的升高而增加。气化持续时间和水蒸气与固体燃料的比例表明,反应器温度低于700℃时,反应速率逐渐变慢。结果表明,不应在反应器温度低于700℃的条件下对油棕残留物进行蒸汽气化,因为每单位质量的样品会消耗大量蒸汽,以气化残留的焦炭。

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