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Hydrogen-rich fuel gas production from refuse plastic fuel pyrolysis and steam gasification

机译:垃圾塑料燃料热解和蒸汽气化生产富氢燃气

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In this study, experimental conditions were optimized to maximize the production of hydrogen gas from refuse plastic fuel (RPF) by pyrolysis and steam gasification processes conducted in a laboratory-scale reactor. We carried out gasification using 10-g RPF samples at different temperatures (700°-1000℃) with and without steam. The effect of the amount of steam (0-0.25 g/min) for RPF steam gasification was also studied. The effect of K_2CO_3 as a catalyst on these processes was also investigated. Experimental results showed that the hydrogen gas yield increased with temperature; with respect to the gas composition, the hydrogen content increased mainly at the expense of other gaseous compounds, which highlights the major extension of secondary cracking reactions in the gaseous fraction at higher temperatures.
机译:在这项研究中,优化了实验条件,以通过在实验室规模的反应器中进行的热解和蒸汽气化工艺,最大程度地利用垃圾塑料燃料(RPF)产生氢气。我们使用10 g RPF样品在不同温度(700°-1000℃)下有或没有蒸汽进行气化。还研究了蒸汽量(0-0.25 g / min)对RPF蒸汽气化的影响。还研究了K_2CO_3作为催化剂对这些过程的影响。实验结果表明,氢气产率随温度的升高而增加。就气体组成而言,氢含量的增加主要是以其他气态化合物为代价的,这突出了在较高温度下气态馏分中二次裂化反应的主要延伸。

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