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Thermal arc plasma gasification of waste glycerol to syngas

机译:热弧等离子体气化废甘油至合成气

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摘要

In this experimental study, waste glycerol gasification to syngas was investigated by utilizing direct current thermal arc plasma of 46-62 kW power. Two gasifying mediums were used: water vapor and air. The plasmachemical reactor capacity exceeded up to 39 kg/h. Glycerol gasification to synthesis gas process was evaluated in terms of the H-2/CO ratio, H-2 and CO yield, energy conversion efficiency, carbon conversion efficiency, and specific energy requirements. Experimental results were compared between and also with other research work. Water vapor used as the main gasifying medium for waste glycerol utilization to syngas demonstrated a higher process performance over the air used. Full waste glycerol conversion to synthesis gas was achieved for the case of water vapor, whereas that in the case of air gasification only 75.7%. The lower heating value of the produced syngas exceeded 9.82 MJ/Nm(3) and 7.32 MJ/Nm(3) for the water vapor plasma and air plasma gasification, respectively. The energy conversion efficiency was calculated to be higher for the water vapor used as a gasifying agent exceeding 63.86%, whereas that of the air plasma gasification only 43.64%. The specific energy consumption required to treat one kilogram of waste glycerol in the environment of water vapor plasma accounted to 191.6 kJ/mol and 266.45 kJ/mol for the air plasma treatment. As conclusion, it was demonstrated that syngas can be successfully produced from waste glycerol by both water vapor and air plasma gasification. However, the use of water vapor as a gasifying agent gave a better process efficiency over the air in all the parameters studied.
机译:在该实验研究中,通过利用46-62 kW功率的直流热弧等离子体来研究对合成气的废甘油气化。使用了两个气化介质:水蒸气和空气。浆液反应器容量超过39千克/小时。根据H-2 / Co比,H-2和CO屈服,能量转换效率,碳转换效率和特定能量要求,评价甘油气化对合成气体过程。比较实验结果与其他研究工作相比。用作用于废甘油利用的主要气化介质的水蒸气在使用的空气中表现出更高的过程性能。对于水蒸气的情况,实现了全废甘油转化为合成气,而在空气气化的情况下,仅为75.7%。对于水蒸气等离子体和空气等离子体气化,所产生的合成气的较低的加热值分别超过9.82mJ / nm(3)和7.32mJ / nm(3)。计算能量转换效率以更高的水蒸气,其用于气化剂超过63.86%,而空气等离子体的气体蒸气仅为43.64%。在水蒸气等离子体环境中处理一千克废甘油所需的具体能耗占191.6kJ / mol和266.45 kJ / mol的空气等离子体处理。结果,证明了合成气可以通过水蒸气和空气等离子体气化从废甘油中成功生产。然而,在研究中的所有参数中,使用水蒸气作为气化剂在空气中产生了更好的工艺效率。

著录项

  • 来源
    《Applied Energy》 |2019年第2期|113306.1-113306.8|共8页
  • 作者单位

    Lithuanian Energy Inst Plasma Proc Lab Breslaujos Str 3 LT-44403 Kaunas Lithuania;

    Lithuanian Energy Inst Plasma Proc Lab Breslaujos Str 3 LT-44403 Kaunas Lithuania;

    Lithuanian Energy Inst Plasma Proc Lab Breslaujos Str 3 LT-44403 Kaunas Lithuania;

    Lithuanian Energy Inst Plasma Proc Lab Breslaujos Str 3 LT-44403 Kaunas Lithuania;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Water vapor; Air; Thermal arc plasma; Gasification; Glycerol; Syngas;

    机译:水蒸气;空气;热弧等离子体;气化;甘油;合成气;

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