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Investigation of simultaneous removal of ammonia and hydrogen sulphide from producer gas in biomass gasification by titanomagnetite

机译:钛磁铁矿气化生物质气化同时去除煤气中氨和硫化氢的研究

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摘要

A novel hot gas cleaning process using titanomagnetite for the simultaneous removal of ammonia (NH_3) and hydrogen sulphide (H_2S) from a producer gas in biomass gasification has been developed. In a hot reactor operated at 500-800 ℃ and under atmospheric pressure, NH_3 is removed by a decomposition reaction to N_2 and H_2, whereas H_2S is removed by an adsorption reaction. Titanomagnetite was tested using three different gas streams, namely 2000 ppmv NH_3 in Ar, 2000 ppmv NH_3 and 230 ppmv H_2S in Ar, and 2000 ppmv NH_3 and 230 ppmv H_2S in a simulated biomass producer gas. From the experimental results, it was discovered that ferrite (α-Fe) was readily formed by the H_2 reduction of titanomagnetite and that almost complete decomposition of NH_3 (100%) was achieved in Ar gas at 700 and 800 ℃. The presence of H_2S in a gas mixture of NH_3 and Ar slightly reduced the catalytic activity for NH_3 decomposition at 700 and 800 ℃ (>96%), and H_2S adsorption of greater than 98% could be achieved in the same temperature range. Under the coexistence of a simulated biomass producer gas, the NH_3 decomposition rate and H_2S adsorption rate were decreased at 800 ℃, which could be due to the high content of H_2 (45 vol%) in the feed gas that favours the reverse reaction of NH_3 decomposition and H_2S adsorption, the increased surface coverage of the active α-Fe phase by adsorbed hydrogen, and the competition of α-Fe for the reverse water-gas shift reaction. Moreover, it was discovered that temperature significantly affected the removal of NH_3 and H_2S in the simulated biomass producer gas and thus the operation temperature needs to be optimised.
机译:开发了一种新颖的利用钛磁铁矿同时去除生物质气化炉煤气中氨(NH_3)和硫化氢(H_2S)的热气的方法。在500-800℃,大气压下运行的热反应器中,NH_3通过与N_2和H_2的分解反应除去,而H_2S通过吸附反应除去。使用三种不同的气流测试了钛磁铁矿,即在Ar中的2000 ppmv NH_3,在Ar中的2000 ppmv NH_3和230 ppmv H_2S,以及在模拟的生物质产生器气体中的2000 ppmv NH_3和230 ppmv H_2S。从实验结果发现,通过钛磁铁矿的H_2还原H_2容易形成铁素体(α-Fe),并且在700和800℃的Ar气体中几乎完全分解了NH_3(100%)。 NH_3和Ar的混合气体中H_2S的存在会稍微降低700和800℃下NH_3分解的催化活性(> 96%),并且在相同温度范围内H_2S的吸附率可达到98%以上。在模拟的生物质产生气共存下,NH_3分解速率和H_2S吸附速率在800℃时降低,这可能是由于进料气中H_2(45 vol%)的含量较高而有利于NH_3的逆反应分解和H_2S吸附,吸附的氢增加了活性α-Fe相的表面覆盖率,以及α-Fe在逆水煤气变换反应中的竞争。此外,还发现温度显着影响模拟生物质生产气中NH_3和H_2S的去除,因此需要优化操作温度。

著录项

  • 来源
    《Fuel》 |2014年第1期|235-242|共8页
  • 作者单位

    Department of Chemical and Process Engineering, College of Engineering, University of Canterbury, Christchurch, New Zealand;

    Department of Chemical and Process Engineering, College of Engineering, University of Canterbury, Christchurch, New Zealand;

    Department of Chemical and Process Engineering, College of Engineering, University of Canterbury, Christchurch, New Zealand;

    Centre for Energy Technology, School of Chemical Engineering, University of Adelaide, South Australia, Australia;

    Department of Chemical and Process Engineering, College of Engineering, University of Canterbury, Private Bag 4800, Christchurch, New Zealand;

  • 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

    Ammonia decomposition; Hydrogen sulphide adsorption; Hot gas cleaning; Iron catalyst; Biomass gasification;

    机译:氨分解;硫化氢吸附;热气清洁;铁催化剂;生物质气化;

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