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首页> 外文期刊>Journal of Energy Resources Technology >Effect of Heat Flux Distribution Profile on Hydrogen Concentration in an Allothermal Downdraft Biomass Gasification Process: Modeling Study
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Effect of Heat Flux Distribution Profile on Hydrogen Concentration in an Allothermal Downdraft Biomass Gasification Process: Modeling Study

机译:热流向下分布生物质气化过程中热通量分布曲线对氢浓度的影响:建模研究

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摘要

Considering the potential of using concentrating solar power systems to supply the heat required for the allothermal gasification process, this study analyzes hydrogen production in such a system by assuming typical radiative heat flux profiles for a receiver of a central tower concentrated solar power (CSP) plant. A detailed model for allothermal gasification in a downdraft fixed bed tubular reactor is proposed. This considers solid and gas phases traveling in parallel flow along the reactor. Results for temperature and gas profile show a reasonable quantitative agreement with experimental works carried out under similar conditions. Aiming to maximize H-2 yield, eight Gaussian flux distributions, similar to those typical of CSP systems, each with a total power of 8 kW (average heat flux 20 kW/m(2)), but with varying peak locations, were analyzed. The results show a maximum producer gas yield and a chemical efficiency of 134.1 kmol/h and 45.9% respectively, with a molar concentration of 47.2% CO, 46.9% H-2, 3.3% CH4, and 2.6% CO2 for a distribution peak at z = 1.4 m, thus relatively close to the flue gas outlet. Hydrogen production and gas yield using this configuration were 4% and 2.9% higher than the achieved using the same power but homogeneously distributed. Solar to chemical efficiencies ranged from 38.9% to 45.9%, with a minimum when distribution peak was at the reactor center. These results are due to high temperatures during the latter stage of the process favoring char gasification reactions.
机译:考虑到使用聚光太阳能系统提供地热气化过程所需热量的潜力,本研究通过假设中央塔式聚光太阳能(CSP)装置接收器的典型辐射热通量分布图,分析了该系统中的氢气产生。提出了下沉式固定床管式反应器中变热气化的详细模型。这考虑了沿反应器平行流动的固相和气相。温度和气体分布的结果与在类似条件下进行的实验工作显示出合理的定量一致性。为了最大化H-2产量,分析了八种高斯通量分布,类似于CSP系统的典型分布,每种分布的总功率为8 kW(平均热通量为20 kW / m(2)),但峰位置不同。结果显示最大产生气产量和化学效率分别为134.1 kmol / h和45.9%,摩尔浓度为47.2%CO,46.9%H-2、3.3%CH4和2.6%CO2的分布峰位于z = 1.4 m,因此相对靠近烟气出口。使用这种配置的氢气产量和气体产率分别比使用相同功率但均匀分布的氢气和天然气的产量高4%和2.9%。太阳到化学的效率在38.9%至45.9%的范围内,当分布峰值位于反应堆中心时最低。这些结果归因于在该过程的后期有利于炭气化反应的高温。

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  • 来源
    《Journal of Energy Resources Technology》 |2019年第3期|031801.1-031801.10|共10页
  • 作者单位

    Univ Norte, Dept Mech Engn, Km 5 Via Puerto Colombia, Barranquilla 081007, Colombia|Inst Univ Pascual Bravo, Dept Mech Engn, Calle 73 73A-226, Medellin 050034, Colombia;

    Univ Sao Paulo, Fac Anim Sci & Food Engn, Dept Biosyst Engn, Ave Duque Caxias Norte 225, BR-13635900 Pirassununga, SP, Brazil;

    Univ Sao Paulo, Fac Anim Sci & Food Engn, Dept Biosyst Engn, Ave Duque Caxias Norte 225, BR-13635900 Pirassununga, SP, Brazil;

    Univ Norte, Dept Mech Engn, Km 5 Via Puerto Colombia, Barranquilla 081007, Colombia;

    Univ Norte, Dept Mech Engn, Km 5 Via Puerto Colombia, Barranquilla 081007, Colombia;

  • 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
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