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Numerical Study of the Pyrolysis of Ellipsoidal Low-Rank Coal Briquettes

机译:椭圆低阶煤球热解的数值研究

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摘要

Low-rank coal (LRC) upgrading is essential to convert LRC to a more thermal-efficient and environmentally friendly fuel before utilization in coal-based industries. Briquetting and pyrolysis are the dominant route, where briquettes are usually in the shape of an ellipsoid through a two-roll briquetting process. In this work, an integrated numerical model is developed to predict the pyrolysis process of ellipsoidal LRC briquettes in a packed-bed pyrolyzer. A computational fluid dynamics (CFD) model is developed to describe the flow and thermochemical behaviors related to the pyrolysis of ellipsoidal LRC briquettes, including dewatering, pyrolysis, and other homo- and heterogeneous chemical reactions. A discrete element method (DEM) model is used to describe the packing density distribution of ellipsoidal briquettes. The model is validated against the measurements in a pilot-scale test rig in terms of the temperature history and gas species yields. Typical in-furnace phenomena are illustrated, including flow field, temperature field, and product evolution. Then, the effects of key variables, including briquette properties and heating conditions, on the pyrolysis behavior are investigated quantitatively. The effects of key parameters, including briquette moisture, final pyrolysis temperature, and briquette aspect ratio, on pyrolysis are studied, and the optimal values are identified under the given conditions. For example, more H-2 and less CH4 are generated when the moisture content of initial briquettes is increased in the range of 2-15%, but in the range of 15-20%, H-2 is then decreased and CH4 is increased. The maximum packing density is obtained when the aspect ratio of briquettes is 2.0. However, the highest temperature increase rate is observed when the aspect ratio is 1.7. An appropriate final pyrolysis temperature, 973 K in this study, is suggested to balance the pyrolysis rate and energy consumption. This model provides a cost-effective tool for optimizing the design and operation of pyrolyzers for ellipsoidal LRC briquettes.
机译:低阶煤(LRC)升级对于在将LRC转换为基于煤炭的行业之前,将其转换为热效率更高,更环保的燃料至关重要。压块和热解是主要途径,其中压块通常通过两辊压块过程呈椭圆形。在这项工作中,建立了一个集成的数值模型来预测在填充床热解器中椭圆形LRC团块的热解过程。建立了计算流体动力学(CFD)模型,以描述与椭圆形LRC团块热解有关的流动和热化学行为,包括脱水,热解以及其他均相和异相化学反应。用离散元法(DEM)模型描述了球团的堆积密度分布。根据温度历史记录和气体种类产量,对照中试规模的试验设备的测量结果对模型进行了验证。给出了典型的炉内现象,包括流场,温度场和产品演变。然后,定量研究了球团性质和加热条件等关键变量对热解行为的影响。研究了煤球水分,最终热解温度和煤球长径比等关键参数对热解的影响,并在给定条件下确定了最佳值。例如,当初始团块的水分含量在2-15%的范围内增加时,会生成更多的H-2,而CH4会减少,但是在15-20%的范围内,则会降低H-2并增加CH4 。当团块的长径比为2.0时,可获得最大堆积密度。但是,当纵横比为1.7时,观察到最高的升温速度。建议在此研究中将最终热解温度设定为973 K,以平衡热解速率和能耗。该模型提供了一种经济有效的工具,可优化椭圆LRC型团块的热解器的设计和操作。

著录项

  • 来源
    《Energy & fuels》 |2018年第4期|4189-4201|共13页
  • 作者单位

    Univ New South Wales, Sch Chem Engn, Sydney, NSW 2052, Australia;

    Univ New South Wales, Sch Chem Engn, Sydney, NSW 2052, Australia;

    Univ New South Wales, Sch Chem Engn, Sydney, NSW 2052, Australia;

    Univ New South Wales, Sch Chem Engn, Sydney, NSW 2052, Australia;

  • 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 00:39:08

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