首页> 外文期刊>Energy & fuels >Experimental Investigation of Fe-Ni-Al Oxygen Carrier Derived from Hydrotalcite-like Precursors for the Chemical Looping Gasification of Biomass Char
【24h】

Experimental Investigation of Fe-Ni-Al Oxygen Carrier Derived from Hydrotalcite-like Precursors for the Chemical Looping Gasification of Biomass Char

机译:类水滑石前驱体生成的Fe-Ni-Al氧载体对生物质焦化学循环气化的实验研究

获取原文
获取原文并翻译 | 示例
       

摘要

Chemical looping gasification (CLG) of biomass uses the lattice oxygen of oxygen carriers to convert biomass into syngas with a low tar content, high heating value, and low price. It is of key importance to exploit well-dispersed and thermally stable oxygen carriers for the CLG process. In the current work, a series of oxygen carriers with varied Fe and Ni molar ratios were synthesized from hydrotalcite compound precursors (HTlcs), which made the metallic elements mix at the molecular level. Consequently, highly dispersed complex metal oxygen carriers can be achieved after precursor calcinations. CLG of biomass char was carried out in TGA and a fixed bed reactor accompanied by various physical and chemical analyses for the fresh and used oxygen carriers. The result manifested the HTlcs crystalline form, which was formed in the precursors and produced the Fe(0.99)Ni(0.6)A(1.1)O(4) compound after calcination, suggesting that a high degree dispersion of the multimetal oxygen carrier was synthesized. The main H-2 uptake and CLG reactivity of the oxygen carriers were related to its higher metal dispersion and synergistic effect between Fe and Ni. Accordingly, there was an optimum Fe/Ni ratio of 4:1 in oxygen carriers at which the oxygen carrier can achieve better CLG reactivity. Also, the oxygen carrier to biomass char mass ratio of 7:3 provided a maximum weight loss of 35.59% and a largest mass loss rate of 2.46 wt %/min, suggesting higher lattice oxygen releasing efficiency. CO exhibited a higher generating rate in the CLG reactions owing to its higher reaction activation energy with lattice oxygen [0], while H-2 was more prone.to being consumed. The morphological analysis of fresh and regenerated samples exhibited that the oxygen carrier was reduced to the Fe3Ni2 alloy phase after the CLG process, and the lattice oxygen can be fully recovered in an air atmosphere. Although the BET surface displayed a decreased trend in the regenerated oxygen carriers, serious sintering was not observed in the samples, and the main metallic crystallized phases were still maintained.
机译:生物质的化学循环气化(CLG)使用氧气载体的晶格氧将生物质转化为具有低焦油含量,高热值和低价格的合成气。对于CLG工艺,利用分散良好且热稳定的氧气载体至关重要。在当前的工作中,从水滑石化合物前体(HTlcs)合成了一系列具有不同Fe和Ni摩尔比的氧载体,这使金属元素在分子水平上混合。因此,在前体煅烧之后,可以获得高度分散的复合金属氧载体。在TGA和固定床反应器中进行生物质炭的CLG,并进行各种物理和化学分析,以分析新鲜和用过的氧气载体。结果表明,HTlcs晶形形成于前体中,并在煅烧后生成Fe(0.99)Ni(0.6)A(1.1)O(4)化合物,表明合成了高度分散的多金属氧载体。氧载体的主要H-2吸收和CLG反应性与其较高的金属分散性以及铁和镍之间的协同作用有关。因此,在氧载体中Fe / Ni的最佳比例为4:1,在该比率下氧载体可以实现更好的CLG反应性。而且,氧载体与生物质炭的质量比为7:3提供了最大的重量损失35.59%和最大的质量损失速率2.46 wt%/ min,表明更高的晶格氧释放效率。一氧化碳在CLG反应中表现出较高的生成速率,这是由于其与晶格氧[0]的反应活化能更高,而H-2则更容易被消耗。新鲜和再生样品的形态分析表明,在CLG工艺之后,氧载体还原为Fe3Ni2合金相,并且在空气中可以完全回收晶格中的氧。尽管BET表面在再生的氧气载体中显示出降低的趋势,但是在样品中未观察到严重的烧结,并且仍然保持了主要的金属结晶相。

著录项

  • 来源
    《Energy & fuels》 |2017年第5期|5174-5182|共9页
  • 作者单位

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China|Taiyuan Univ Technol, State Key Lab Breeding Base Coal Sci & Technol, Shanxi Prov & Minist Sci & Technol, Taiyuan 030024, Peoples R China;

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China;

    Guangdong Mech & Elect Coll, Guangzhou 510515, Guangdong, Peoples R China;

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China;

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China;

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China;

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China;

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China;

    Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China|CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China;

  • 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
  • 关键词

  • 入库时间 2022-08-18 00:39:33

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号