可再生能源2024,Vol.42Issue(2) :143-150.

吸附强化生物质蒸汽重整气化制氢的热力学研究

Thermodynamic study on adsorption enhanced biomass steam reforming gasification for hydrogen production

家丽非 秦梦鑫 邵正日 谢华清 李荣泉
可再生能源2024,Vol.42Issue(2) :143-150.

吸附强化生物质蒸汽重整气化制氢的热力学研究

Thermodynamic study on adsorption enhanced biomass steam reforming gasification for hydrogen production

家丽非 1秦梦鑫 1邵正日 2谢华清 1李荣泉1
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作者信息

  • 1. 东北大学 冶金学院, 辽宁 沈阳 110819
  • 2. 营口理工学院 辽宁省储能与能源利用技术重点实验室,辽宁 营口 115000
  • 折叠

摘要

文章利用Aspen Plus流程模拟软件对比研究了在不同条件[气化温度、水与生物质中碳的物质的量比(S/C)、反应压力等]下,是否添加CO2 吸附剂对生物质蒸汽重整气化制氢的影响.以制取单位体积氢气所需的能耗和物耗为考察指标,利用矩阵分析方法进行优化,得到吸附强化生物质蒸汽重整气化的最佳条件:气化温度为 500℃,S/C=2,气化压力为 0.1 MPa,在此条件下,氢气产量为 1.56 m3/kg,氢气浓度为 98.3%,制取单位体积氢气所需的能耗和物耗分别为4.16 MJ/m3 和0.64 kg/m3.

Abstract

In this paper,Aspen Plus process simulation software was used to compare the effects of adding CO2 adsorbent on hydrogen production by steam reforming of biomass under different conditions[gasification temperature,mass ratio of water to carbon in biomass(S/C),reaction pressure].Based on the energy consumption and material consumption required for producing hydrogen per unit volume,the matrix analysis method was used to optimize,and the best conditions of adsorption enhanced biomass steam reforming gasification were obtained:When the gasification temperature is 500℃,S/C=2 and the gasification pressure is 0.1 MPa,under this condition,the hydrogen production is 1.56 m3/kg,the hydrogen concentration is 98.3%,and the energy consumption and material consumption required for producing the unit volume of hydrogen are 4.16 MJ/m3 and 0.64 kg/m3,respectively.

关键词

生物质/吸附强化/蒸汽气化/氢气

Key words

biomass/adsorption enhancement/steam gasification/hydrogen

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基金项目

中央高校基本科研业务费专项(N2225043)

出版年

2024
可再生能源
辽宁省能源研究所 中国农村能源行业协会 中国资源综合利用协会可再生能源专委会 中国生物质能技术开发中心 辽宁省太阳能学会

可再生能源

CSTPCD北大核心
影响因子:0.605
ISSN:1671-5292
参考文献量4
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