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首页> 外文期刊>Fuel >An integrated process for the production of lignocellulosic biomass pyrolysis oils using calcined limestone as a heat carrier with catalytic properties
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An integrated process for the production of lignocellulosic biomass pyrolysis oils using calcined limestone as a heat carrier with catalytic properties

机译:使用煅烧石灰石作为具有催化特性的热载体生产木质纤维素生物质热解油的综合工艺

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摘要

The production of upgraded bio-oils by an integrated process using a mixture of calcined limestone and sand as a heat carrier with catalytic properties was experimentally studied at pilot scale. The integrated process consisted of two main steps: biomass catalytic pyrolysis in an Auger reactor for bio-oil production and char combustion in a fluidised-bed combustor for heat carrier heating and regeneration. A temperature of 450 degrees C was fixed as an optimum value to carry out the catalytic pyrolysis step. Temperatures ranging from 700 to 800 degrees C were assessed in the char combustor. Process simulation demonstrated that solid recirculation from the combustor to the pyrolysis reactor was marginally affected in this temperature range. However, an optimum char combustion temperature of 800 degrees C was selected from an environmental point of view, since lower polyaromatic emissions were detected whilst NOx emissions were kept under the legislation limits. Under designated conditions, several pyrolysis-combustion cycles were carried out. A moderate deactivation of the catalyst by partial carbonation was found. This fact makes necessary the incorporation of a purge and an inlet of fresh heat carrier in order to maintain the bio-oil quality in the integrated process. (C) 2016 Elsevier Ltd. All rights reserved.
机译:在中试规模上对通过煅烧石灰石和沙子的混合物作为具有催化性能的热载体的集成工艺生产升级的生物油进行了实验研究。集成过程包括两个主要步骤:在俄歇反应器中进行生物质催化热解以生产生物油,以及在流化床燃烧器中进行焦炭燃烧以进行热载体加热和再生。将450℃的温度固定为最佳值以进行催化热解步骤。在炭燃烧器中评估了700至800摄氏度的温度。过程仿真表明,在该温度范围内,从燃烧室到热解反应器的固体再循环受到了很小的影响。但是,从环境的角度出发,选择最佳的炭燃烧温度为800摄氏度,因为检测到了较低的多芳烃排放量,而氮氧化物的排放量却保持在法律规定的范围内。在指定条件下,进行了几次热解燃烧循环。发现通过部分碳酸化使催化剂适度失活。这一事实使得必须结合吹扫和新鲜热载体的入口,以便在集成过程中保持生物油的质量。 (C)2016 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Fuel》 |2016年第1期|430-437|共8页
  • 作者单位

    CSIC, Inst Carboquim ICB, C Miguel Luesma 4, Zaragoza 50018, Spain;

    CSIC, Inst Carboquim ICB, C Miguel Luesma 4, Zaragoza 50018, Spain;

    CSIC, Inst Carboquim ICB, C Miguel Luesma 4, Zaragoza 50018, Spain;

    CSIC, Inst Carboquim ICB, C Miguel Luesma 4, Zaragoza 50018, Spain;

    CSIC, Inst Carboquim ICB, C Miguel Luesma 4, Zaragoza 50018, Spain;

  • 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

    Biomass; Catalytic pyrolysis; Char combustion; Auger reactor; Fluidised-bed reactor;

    机译:生物质;催化热解;焦炭燃烧;螺旋反应器;流化床反应器;

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