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Hydrogen and syngas production from catalytic steam gasification of char derived from ion-exchangeable Na- and Ca-loaded coal

机译:碳和离子交换性煤制焦炭的催化蒸汽气化制氢和合成气

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摘要

Catalytic steam gasification of char derived from low-rank coal possesses substantial potential as a source of hydrogen energy and syngas feedstocks, and its performances are largely associated with the employed catalysts. Therein, ion-exchangeable Na or Ca species are always regarded as excellent in-situ catalysts in low-rank coal. In this paper, gasification of Na-Char, Ca-Char and a Na/Ca-Char mixture with different partial pressures of steam was performed within a temperature range of 700-900 degrees C using a micro fluidized bed reaction analyzer. The results indicate that Na and Ca species could accelerate the gas release rate during gasification and even significantly increase H-2 production, in sharp contrast to non-catalytic gasification. Variations in the product gases during Na-Char and Ca-Char gasification were completely different, which associated with the different deactivation pathways and catalytic reaction mechanisms of Na and Ca catalysts. With an increasing gasification temperature, the decreasing trend of H-2 production for Na-Char gasification was mainly due to the loss of Na during gasification. Conversely, the enhancement of Ca activity promoted the H-2 production. The H-2/CO ratio of Ca-Char gasification at 700 degrees C approximately ranged from 1.0 to 2.0 as a function of the partial pressure of steam, which suggested catalytic gasification can be suitable for hydrogen-rich production and subsequent synthesis reactions. In addition, gasification of Na/Ca-Char mixture produced a higher hydrogen content in the product gases than that of Na-Char or Ca-Char gasification alone, particularly for the 30%Na/70%Ca-Char mixture. It implies that the high H-2 production of 70%Ca30%Na-Char mixture was attributed to the cooperative effects of the Na and Ca species on the catalytic activity. This study provides comprehensive information regarding the effects of ion-exchangeable Na, Ca and a Na/Ca mixture on the hydrogen production and syngas composition during steam gasification, which provides new insight into the utilization of low-rank coal. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:低级煤衍生的焦炭的催化蒸汽气化具有巨大的潜力,可作为氢能和合成气原料的来源,其性能在很大程度上与所使用的催化剂有关。其中,离子交换性Na或Ca一直被认为是低阶煤中出色的原位催化剂。在本文中,使用微流化床反应分析仪在700-900摄氏度的温度范围内,将水蒸气分压不同的Na-Char,Ca-Char和Na / Ca-Char混合物气化。结果表明,与非催化气化形成鲜明对比的是,Na和Ca物种可以加快气化过程中的气体释放速率,甚至显着增加H-2的产生。 Na-Char和Ca-Char气化过程中产物气体的变化完全不同,这与Na和Ca催化剂的不同失活途径和催化反应机理有关。随着气化温度的升高,Na-Char气化过程中H-2产量的下降趋势主要是由于气化过程中Na的损失。相反,Ca活性的增强促进了H-2的产生。 Ca-Char气化在700摄氏度下的H-2 / CO比值随蒸汽分压的变化而变化,大约为1.0至2.0,这表明催化气化可适用于富氢生产和后续的合成反应。另外,与单独的Na-Char或Ca-Char气化相比,Na / Ca-Char混合物的气化在产物气体中产生更高的氢含量,特别是对于30%Na / 70%Ca-Char混合物。这暗示了70%Ca30%Na-Char混合物的高H-2产生归因于Na和Ca物种对催化活性的协同作用。这项研究提供了有关离子可交换的Na,Ca和Na / Ca混合物对蒸汽气化过程中氢气产生和合成气组成的影响的全面信息,这为低等级煤的利用提供了新见识。 (C)2018氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

著录项

  • 来源
    《International journal of hydrogen energy》 |2018年第27期|12034-12048|共15页
  • 作者单位

    Harbin Inst Technol, Sch Energy Sci & Engn, 92 West Dazhi St, Harbin 150001, Heilongjiang, Peoples R China;

    Harbin Inst Technol, Sch Energy Sci & Engn, 92 West Dazhi St, Harbin 150001, Heilongjiang, Peoples R China;

    Harbin Inst Technol, Sch Energy Sci & Engn, 92 West Dazhi St, Harbin 150001, Heilongjiang, Peoples R China;

    Harbin Inst Technol, Sch Energy Sci & Engn, 92 West Dazhi St, Harbin 150001, Heilongjiang, Peoples R China;

  • 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

    Hydrogen; Gasification; Char; Catalysis; Zhundong coal;

    机译:氢气;气化;焦炭;催化;准东煤;

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