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Sulfur Abatement in Pyrolysis of Straw Pellets

机译:秸秆颗粒热解中的硫减少

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A batch-type reactor was used to study the sulfur release from pellets made of Danish wheat straw during inert conditions. In addition, two means of sulfur abatement were investigated, the use of calcium-based additives for sulfur retention and the use of nonthermal plasma (NTP) for the treatment of the devolatilized products. The results were interpreted by quantifying the releases of hydrogen sulfide (H_2S) and carbonyl sulfide (COS) to the gas phase for the pyrolysis temperatures of 400-800 ℃. In experiments where additives were used, straw was mixed and pelletized with either calcium oxide (CaO) or calcium hydroxide [Ca(OH)_2] at different calcium/sulfur ratios. The effect of additives on the sulfur release was difficult to assess by solely investigating the gaseous products. However, a comparison of the sulfur content in the starting material and the char residues after pyrolysis showed evidence of minor sulfur retention. The nonthermal plasma reactor system was set up to process the produced gas either before or after the removal of the liquid fraction from the devolatilized products. Furthermore, carbon dioxide was mixed with the nitrogen carrier gas to achieve a more complex gas composition for the nonthermal plasma. For comparative reasons, some preliminary experiments were performed to study the removal efficiency of H_2S in pure nitrogen. The removal efficiency for sulfur under the effect of nonthermal plasma in pure N_2 increased with an increasing H_2S concentration and plasma power. The highest registered removal efficiency was close to 96%. The removal efficiency of H_2S in the pyrolysis experiments was highest at a pyrolysis temperature of 400 ℃, with the nonthermal plasma reactor placed downstream of liquid removal. At this configuration, 86% of H_2S was removed from the devolatilized products. The best plasma reactor placement was proved to be downstream of liquid removal for both H_2S and COS. Increasing the CO_2 amount in the carrier gas has improved the removal efficiency of H_2S at the cost of increased COS formation.
机译:间歇式反应器用于研究在惰性条件下丹麦小麦秸秆制粒中硫的释放。此外,研究了两种减少硫的方法,一种是使用钙基添加剂来保留硫,另一种是使用非热等离子体(NTP)处理脱挥发分的产品。在400-800℃的热解温度下,通过量化硫化氢(H_2S)和羰基硫化物(COS)向气相的释放可以解释结果。在使用添加剂的实验中,将秸秆混合并以不同的钙/硫比与氧化钙(CaO)或氢氧化钙[Ca(OH)_2]造粒。仅通过研究气态产物很难评估添加剂对硫释放的影响。但是,将原料中的硫含量和热解后的焦炭残留物进行比较,表明硫保留较少。设置非热等离子体反应器系统以在从脱挥发分的产物中除去液体馏分之前或之后处理产生的气体。此外,将二氧化碳与氮气载气混合以获得用于非热等离子体的更复杂的气体组成。出于比较的原因,进行了一些初步实验以研究H_2S在纯氮中的去除效率。在非热等离子体作用下,纯N_2对硫的去除效率随H_2S浓度和等离子体功率的增加而增加。注册的最高清除效率接近96%。在400℃的热解温度下,热解实验中H_2S的去除效率最高,非热等离子体反应器位于液体去除的下游。在这种配置下,从脱挥发分的产物中除去了86%的H_2S。事实证明,对于H_2S和COS而言,最佳的等离子体反应器放置都在液体去除的下游,增加载气中的CO_2量以增加COS形成为代价提高了H_2S的去除效率。

著录项

  • 来源
    《Energy & fuels》 |2008年第4期|p.2789-2795|共7页
  • 作者单位

    Norwegian University of Science and Technology, NO-7491, Trondheim, Norway, and Sintef Energy Research, NO-7465, Trondheim, Norway;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 TK-;
  • 关键词

  • 入库时间 2022-08-18 00:42:39

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