1.北京科技大学能源与环境工程学院, 北京 100083
2.北京科技大学顺德创新学院, 广东 佛山 528399
3.钢铁工业环境保护全国重点实验室, 北京 102600
张洁涵(1997—),女,博士研究生,zjh9341@163.com
李诗媛(1979—),女,博士,教授,lishiyuan@ustb.edu.cn
收稿:2026-01-19,
修回:2026-05-20,
录用:2026-05-28,
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张洁涵, 王书麟, 王光绪, 等. H2/CO流态化还原铁矿粉气固反应特性研究[J/OL]. 化工学报, 2026. DOI: 10.11949/0438-1157.20260084.
ZHANG Jiehan, WANG Shulin, WANG Guangxu, et al. Study on gas-solid reaction characteristics of H2/CO fluidized reduction of iron ore powder[J/OL]. CIESC Journal, 2026. DOI: 10.11949/0438-1157.20260084.
张洁涵, 王书麟, 王光绪, 等. H2/CO流态化还原铁矿粉气固反应特性研究[J/OL]. 化工学报, 2026. DOI: 10.11949/0438-1157.20260084. DOI:
ZHANG Jiehan, WANG Shulin, WANG Guangxu, et al. Study on gas-solid reaction characteristics of H2/CO fluidized reduction of iron ore powder[J/OL]. CIESC Journal, 2026. DOI: 10.11949/0438-1157.20260084. DOI:
本研究基于等效特征图谱的质谱定量方法,采用微型流化床反应器,系统探究了还原温度、铁矿粉成分及H
2
/CO混合比例对铁矿粉流化床直接还原全过程的影响(即从反应开始至结束,还原度/速率实时演化过程)。通过实时解析H
2
/CO/H
2
O
(g)
/CO
2
四种气体的质量流量,准确获取了H
2
与CO的实时还原贡献率、还原速率、气体利用率及全过程还原度,并结合中间体与产物的晶相、形貌与粒径分析,揭示了混合气体的还原行为差异。结果表明:升高温度有助于提升还原度与气体利用率,但温度超过800 ℃时对还原度的提高有限且加剧颗粒粘结。在矿物组成方面,流化床工艺更适用于粘结性低、还原性高的AQ矿种(赤铁矿),与DC(磁铁矿)和BX(高FeO)矿种相比,AQ样品还原后颗粒粒径降低30%,还原度提高10%以上。混合还原时,随着H
2
比例从30%增至70%,还原机制由初期的CO占主导转变为H
2
在整个还原阶段起主导作用;当H
2
比例超过50%时,其还原速率和还原贡献率均为CO的2倍以上,表现出显著的扩散和还原活性优势。
In order to surmount the dual impediments of quantifying the contribution of mixed gas reduction in hydrogen metallurgy and the important problem of particle bonding in fluidized bed process
this study systematically investigated the effects of reduction temperature (700-850 °C)
iron ore composition and content (mainly differences in FeO and SiO
2
contents)
and H
2
/CO ratio (30-70%) on the entire process of fluidized bed direct reduction of iron (i.e.
the real-time evolution process of reduction degree/rate from the start to the end of the reaction). The study utilized the mass spectrometry quantitative method of equivalent characteristic map
in combination with a micro fluidized bed reactor. A thorough real-time investigation was conducted to ascertain the reduction contribution degree of H
2
and CO
the real-time reduction rates
the gas utilization rates
and the overall reduction degrees. This investigation involved a comprehensive real-time analysis of the mass flow rates of four gases (H
2
/CO/H
2
O
(g)
/CO
2
). The reduction differences of the mixed gas were determined by combining these with the crystal phases
surface morphologies
and particle sizes of the intermediates and products. The findings of the study demonstrated that an increase in reduction temperature led to enhanced reduction degree and gas utilization. However
beyond 800°C
the enhancement in reduction degree became marginal
while particle agglomeration intensified significantly. With regard to mineral composition
the fluidized bed process was particularly wel
l-suited to AQ-type ore (hematite)
which demonstrated low adhesiveness and high reducibility. In comparison with DC (magnetite) and BX (high FeO content) ores
reduced AQ samples demonstrated a 30% decrease in average particle size and attained a final reduction degree that exceeded 10%. In the context of mixed-gas reduction
an increase in the H
2
fraction from 30% to 70% resulted in a shift in the dominant reducing agent from CO in the initial stage to H
2
throughout the reduction process. As the proportion of H
2
exceeded 50%
both the reduction and contribution rates of H
2
surpassed those of CO by more than twice the amount. This demonstrated clear advantages in terms of diffusion kinetics and intrinsic reactivity.
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