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首页> 外文期刊>Applied Energy >Investigation of different manganese ores as oxygen carriers in chemical-looping combustion (CLC) for solid fuels
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Investigation of different manganese ores as oxygen carriers in chemical-looping combustion (CLC) for solid fuels

机译:固体燃料化学循环燃烧(CLC)中作为氧气载体的不同锰矿石的研究

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摘要

The chemical-looping combustion (CLC) process is a novel solution for efficient combustion with direct capture of carbon dioxide. The process uses a metal oxide as an oxygen carrier to transfer oxygen from an air to a fuel reactor, where the fuel reacts with the solid oxygen carrier. In this work, six different manganese ores are investigated as oxygen carriers for CLC application. The chemical-looping characteristics of the oxygen carriers were evaluated in a laboratory-scale fluidized-bed reactor in the temperature range of 900-970 ℃ during alternating reducing and oxidizing conditions. Three of the manganese ores showed a small oxygen release in inert environment between 850 and 950 ℃. During reactivity tests, the gas yield with methane increased with the temperature and complete conversion of 50% CO in H_2 was obtained for all of the ores. The rates of char gasification of two fuels, namely Mexican petroleum coke and Swedish wood char, were compared for the different manganese ores at 970 ℃ and with 50% H_2O in N_2 as fluidizing gas. Ilmenite and a manufactured Mn-oxide oxygen carrier consisting of Mn_3O_4 and MgO-stabilized ZrO_2 as support were also included for comparison. The char gasification rate and the gas conversion were higher with the manganese ores and the Mn-oxide oxygen carrier compared to ilmenite. However, the higher reactivity of the manganese ores with H_2 and the ensuing decrease in H_2 inhibition for manganese ores is not sufficient to explain their higher rate of char gasification. Surface analysis of partially gasified petcoke particles in the presence of manganese ores showed formation of cavities and channels as well as a uniform distribution of potassium and sodium elements. The rate of char gasification also increased with the concentration of potassium and sodium impurities in the manganese ores. Thus the results suggest that the increased rate of char conversion for manganese ores is due to alkali-catalyzed steam gasification. The increase in rate of char gasification, in combination with potentially low costs of these materials suggests that manganese ores could be interesting materials for CLC with solid fuels.
机译:化学循环燃烧(CLC)工艺是一种有效的燃烧方法,可直接捕获二氧化碳,是一种新颖的解决方案。该方法使用金属氧化物作为氧气载体,将氧气从空气中转移到燃料反应器中,在此燃料与固体氧气载体发生反应。在这项工作中,研究了六种不同的锰矿石作为CLC应用的氧气载体。在实验室规模的流化床反应器中,在交替的还原和氧化条件下,于900-970℃的温度范围内,对氧载体的化学环化特性进行了评估。三种锰矿石在850至950℃的惰性环境中显示出少量的氧气释放。在反应性测试过程中,甲烷的气体产率随温度的升高而增加,所有矿石均实现了H_2中50%CO的完全转化。比较了不同锰矿石在970℃和以N_2为50%H_2O作为流化气体时,两种燃料(墨西哥石油焦和瑞典木炭)的炭气化率。为了比较,还包括钛铁矿和由Mn_3O_4和MgO稳定的ZrO_2制成的Mn氧化物氧载体。与钛铁矿相比,锰矿石和锰氧化物氧载体的炭气化率和气体转化率更高。然而,锰矿石与H_2的较高反应性以及随之而来的H_2对锰矿石的抑制作用降低不足以解释其较高的炭化率。在锰矿石存在下,部分气化的石油焦颗粒的表面分析表明,空穴和通道的形成以及钾和钠元素的均匀分布。焦炭气化速率也随着锰矿石中钾和钠杂质的浓度增加而增加。因此,结果表明锰矿石的焦炭转化率提高是由于碱催化的蒸汽气化。焦炭气化速率的提高,加上这些材料的潜在低成本,表明锰矿石可能是使用固体燃料进行CLC的有趣材料。

著录项

  • 来源
    《Applied Energy》 |2014年第1期|1883-1894|共12页
  • 作者单位

    Department of Chemical and Biological Engineering, Division of Environmental Inorganic Chemistry, Chalmers University of Technology, SE-412 96 Coeteborg, Sweden;

    Department of Chemical and Biological Engineering, Division of Environmental Inorganic Chemistry, Chalmers University of Technology, SE-412 96 Coeteborg, Sweden;

    Department of Energy and Environment, Division of Energy Technology, Chalmers University of Technology, SE-412 96 Goeteborg, Sweden;

    Department of Energy and Environment, Division of Energy Technology, Chalmers University of Technology, SE-412 96 Goeteborg, Sweden;

  • 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

    CO_2-capture; Chemical-looping combustion (CLC); Oxygen carrier; Manganese ore; Solid fuel; Catalytic steam gasification;

    机译:二氧化碳捕获化学循环燃烧(CLC);氧气载体锰矿固体燃料;催化蒸汽气化;

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