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FLASHCHAIN Theory for Rapid Coal Devolatilization Kinetics. 10. Extents of Conversion for Hydropyrolysis and Hydrogasification of Any Coal

机译:FLASHCHAIN快速脱挥发分动力学理论。 10.任何煤的加氢热解和加氢气化的转化程度

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摘要

This paper extends FLASHCHAIN theory with mechanisms for (i) hydrogenation of labile bridges in the condensed coal phase which enhance tar yields during primary devolatilization under some, but not all, conditions and (ii) heterogeneous hydrogasification of char into CH4. Under the H-2 pressures associated with entrained coal gasification technology, coal devolatilization at heating rates faster than 10(3) degrees C/s does not provide sufficient time for appreciable bridge hydrogenation so tar yields are not enhanced. Conversely, tar yields under slow heating conditions are strongly enhanced. The mechanisms proposed for bridge hydrogenation and its associated impact on fragment recombination in FLASHCHAIN accurately depict the joint impact of heating rate and H-2 pressure on tar yields. Whereas tar yields from rapid devolatilization diminish for progressively higher pressures, total weight loss remains steady or passes through a minimum at some H-2 pressure around 1 MPa, because char hydrogasification counteracts the lower weight loss associated with diminished tar yields at progressively higher pressures. A single, half-order methanation reaction within the CBK/G framework gave results within the measurement uncertainties through 15 MPa H-2. In combination, the mechanisms for hydropyrolysis and hydrogasification accurately interpreted a database representing coals of rank from lignite to medium volatile bituminous; heating rates from 1 to 10(3) degrees C/s; temperatures from 550 to 1150 degrees C; reaction times to 180 s; and particle diameters to 1 mm. The assigned hydrogasification reactivities are far less variable than those for char gasification by steam and CO2 and show no consistent trend with rank.
机译:本文将FLASHCHAIN理论扩展为以下机制:(i)在某些(但不是全部)条件下,在凝结煤相中不稳定的桥的氢化反应可在一次脱挥发分期间提高焦油收率,以及(ii)将焦炭进行异质加氢气化成CH4。在与夹带煤气化技术相关的H-2压力下,以高于10(3)℃/ s的加热速率进行脱挥发分的煤无法为桥的明显氢化提供足够的时间,因此不会提高焦油收率。相反,在缓慢加热条件下的焦油收率大大提高。提出的桥式加氢机理及其对FLASHCHAIN中片段重组的影响准确地描述了加热速率和H-2压力对焦油收率的共同影响。快速脱挥发分的焦油收率随压力的升高而逐渐降低,而总重量损失保持稳定或在大约1 MPa的某些H-2压力下达到最小值,因为焦炭加氢气化抵消了随着重量逐渐增高而焦油收率下降而导致的重量减轻。 CBK / G框架内的一个单级甲烷化反应在15 MPa H-2的测量不确定度范围内得出结果。结合起来,加氢热解和加氢气化的机理可以准确地解释一个数据库,该数据库代表了从褐煤到中等挥发性沥青的等级煤。加热速率从1到10(3)摄氏度/秒; 550至1150摄氏度的温度;反应时间至180秒;和粒径为1毫米。所指定的加氢气化反应性的可变性远不及通过蒸汽和CO2进行焦化气化的可变性,并且在等级上没有一致的趋势。

著录项

  • 来源
    《Energy & fuels》 |2018年第1期|384-395|共12页
  • 作者

    Niksa Stephen;

  • 作者单位

    Niksa Energy Associates LLC, 1745 Terrace Dr, Belmont, CA 94002 USA;

  • 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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