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Comparing Direct and Indirect Fluidized Bed Gasification: Effect of Redox Cycle on Olivine Activity

机译:直接和间接流化床气化的比较:氧化还原循环对橄榄石活性的影响

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摘要

Fluidized bed gasification processes are generally considered a good choice for biomass and waste because of its fuel flexibility. Furthermore, it is a relatively low-temperature highly efficient process operating at 700-900℃ compared with, for example, coal-based entrained flow processes that mostly operate at 1400-1600℃. Indirect fluidized bed gasification is becoming increasingly popular for some applications due to the possibility of producing a N_2-free gas without the need for an air separation unit, as well as complete conversion of the fuel. ECN has developed MILENA indirect gasification, in which gasification and combustion are physically separated, but both reactors are placed in the same vessel. This article aims to compare the performance of olivine as bed material in direct- and indirect (MILENA) gasification. With this purpose, oxidation/reduction cycles have been simulated in a direct gasifier to determine the effect of olivine preoxidation in terms of tar destruction and oxygen transport. Results show that olivine preoxidation mainly enhances the capacity of oxygen transport of the bed material, which adds up to the catalytic effect of iron in olivine towards tar destruction. Oxygen transport capacity of olivine has been quantified as ER = 0.25 at the maximum initial CO_2 peak, and it has been estimated that 20-25% wt of iron in olivine is able to transfer oxygen during the first 10 min operation. On the other hand, it has been found that MILENA operating conditions are equivalent to the point of initial maximum peak of CO_2 in the devolatilization stage. This means that oxygen transport capacity of olivine is kept at its maximum due to the continuous combustion/gasification cycles, and olivine is kept activated by cyclical migration of iron into the surface and subsequent fast reduction. The effect of oxygen transport on the overall heat balance of the MILENA gasifier is equivalent to oxidation of additional fuel in the combustor.
机译:流化床气化工艺因其燃料的灵活性而被普遍认为是生物质和废物的理想选择。此外,与例如大部分在1400-1600℃下运行的煤基气流床工艺相比,这是一种在700-900℃下运行的相对低温高效工艺。间接流化床气化在某些应用中变得越来越普遍,这是因为无需空气分离装置即可产生不含N_2的气体,以及燃料的完全转化。 ECN开发了MILENA间接气化技术,其中气化和燃烧在物理上是分开的,但是两个反应器都放在同一容器中。本文旨在比较橄榄石在直接和间接(MILENA)气化中作为床层材料的性能。为此目的,已经在直接气化炉中模拟了氧化/还原循环,以确定焦油破坏和氧气输送方面的橄榄石预氧化作用。结果表明,橄榄石的预氧化作用主要增强了床层材料的氧气输送能力,加之橄榄石中铁对焦油破坏的催化作用。在最大的初始CO_2峰值处,橄榄石的氧气传输能力已被量化为ER = 0.25,并且据估计,在最初的10分钟操作中,橄榄石中20-25%wt的铁能够传输氧气。另一方面,已经发现MILENA操作条件等于在脱挥发分阶段的CO 2的初始最大峰值点。这意味着由于连续的燃烧/气化循环,橄榄石的氧气输送能力保持在最大,并且通过铁周期性地迁移到表面并随后快速还原,橄榄石保持活化。氧气输送对MILENA气化炉整体热量平衡的影响等同于燃烧室中其他燃料的氧化。

著录项

  • 来源
    《Environmental progress》 |2014年第3期|711-720|共10页
  • 作者单位

    Energy research Centre of The Netherlands (ECN), Unit Biomass & Energy Efficiency, 1755 ZG Petten,The Netherlands;

    Energy research Centre of The Netherlands (ECN), Unit Biomass & Energy Efficiency, 1755 ZG Petten,The Netherlands;

    Energy research Centre of The Netherlands (ECN), Unit Biomass & Energy Efficiency, 1755 ZG Petten,The Netherlands;

    Energy research Centre of The Netherlands (ECN), Unit Biomass & Energy Efficiency, 1755 ZG Petten,The Netherlands;

    Energy research Centre of The Netherlands (ECN), Unit Biomass & Energy Efficiency, 1755 ZG Petten,The Netherlands;

    Energy research Centre of The Netherlands (ECN), Unit Biomass & Energy Efficiency, 1755 ZG Petten,The Netherlands;

  • 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

    indirect gasification; MILENA gasifier; olivine; catalytic tar destruction; oxygen transport; redox cycle; chemical looping;

    机译:间接气化MILENA气化炉;橄榄石催化焦油破坏;氧气输送氧化还原循环化学循环;
  • 入库时间 2022-08-17 13:28:12

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