Wenlei Zhou, Fuyong Su, Likun Yang, Sizong Zhang, Hailong Huo
{"title":"流化床中铁矿粉的流化行为和氢气还原的 DDPM 模拟","authors":"Wenlei Zhou, Fuyong Su, Likun Yang, Sizong Zhang, Hailong Huo","doi":"10.1007/s11663-024-03205-z","DOIUrl":null,"url":null,"abstract":"<p>In this paper, the hydrogen direct reduction of iron ore fines is numerically studied by using the Dense Discrete Phase Model (DDPM) in the fluidized bed. The fluidization behavior at different inlet gas velocities (<i>U</i><sub>g</sub>) as well as the influence of <i>U</i><sub>g</sub> and hydrogen concentration on reduction degree (<i>RD</i>) are comprehensively investigated. The result indicates the increase of time-averaged solids volume fraction for the same cross-sectional heights with increasing <i>U</i><sub>g</sub> when the bed height (<i>H</i>) exceeds 0.06 m. Furthermore, the reduction rate of mineral powder increases with higher <i>U</i><sub>g</sub> value, and the <i>RD</i> reaches almost 100 pct after 4000 seconds of reduction time with <i>U</i><sub>g</sub> ranging from 0.35 to 0.65 m/s. The reduction rate increases noticeably with the increase of hydrogen concentration in the range of 10 to 100 pct, and Fe<sub>2</sub>O<sub>3</sub> can be completely converted to Fe under condition of 65 pct H<sub>2</sub> concentration after 4000 seconds. Moreover, higher H<sub>2</sub> concentration leads to faster rate of Fe<sub>2</sub>O<sub>3</sub> consumption and Fe production. The mass fraction peak values of Fe<sub>3</sub>O<sub>4</sub> and FeO are in the range of 0.29 to 0.34 and 0.21 to 0.24 under different H<sub>2</sub> concentrations, respectively.</p>","PeriodicalId":18613,"journal":{"name":"Metallurgical and Materials Transactions B","volume":"55 1","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2024-07-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"DDPM Simulation for Fluidization Behavior and Reduction of Iron Ore Fines with Hydrogen in the Fluidized Bed\",\"authors\":\"Wenlei Zhou, Fuyong Su, Likun Yang, Sizong Zhang, Hailong Huo\",\"doi\":\"10.1007/s11663-024-03205-z\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>In this paper, the hydrogen direct reduction of iron ore fines is numerically studied by using the Dense Discrete Phase Model (DDPM) in the fluidized bed. The fluidization behavior at different inlet gas velocities (<i>U</i><sub>g</sub>) as well as the influence of <i>U</i><sub>g</sub> and hydrogen concentration on reduction degree (<i>RD</i>) are comprehensively investigated. The result indicates the increase of time-averaged solids volume fraction for the same cross-sectional heights with increasing <i>U</i><sub>g</sub> when the bed height (<i>H</i>) exceeds 0.06 m. Furthermore, the reduction rate of mineral powder increases with higher <i>U</i><sub>g</sub> value, and the <i>RD</i> reaches almost 100 pct after 4000 seconds of reduction time with <i>U</i><sub>g</sub> ranging from 0.35 to 0.65 m/s. The reduction rate increases noticeably with the increase of hydrogen concentration in the range of 10 to 100 pct, and Fe<sub>2</sub>O<sub>3</sub> can be completely converted to Fe under condition of 65 pct H<sub>2</sub> concentration after 4000 seconds. Moreover, higher H<sub>2</sub> concentration leads to faster rate of Fe<sub>2</sub>O<sub>3</sub> consumption and Fe production. The mass fraction peak values of Fe<sub>3</sub>O<sub>4</sub> and FeO are in the range of 0.29 to 0.34 and 0.21 to 0.24 under different H<sub>2</sub> concentrations, respectively.</p>\",\"PeriodicalId\":18613,\"journal\":{\"name\":\"Metallurgical and Materials Transactions B\",\"volume\":\"55 1\",\"pages\":\"\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2024-07-10\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Metallurgical and Materials Transactions B\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.1007/s11663-024-03205-z\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Metallurgical and Materials Transactions B","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1007/s11663-024-03205-z","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
摘要
本文利用流化床中的致密离散相模型(DDPM)对铁矿粉的氢气直接还原进行了数值研究。全面研究了不同入口气体速度(Ug)下的流化行为,以及 Ug 和氢浓度对还原度(RD)的影响。结果表明,当床高(H)超过 0.06 米时,相同截面高度下的时间平均固体体积分数随 Ug 的增加而增加。此外,矿粉的还原率随 Ug 值的增加而增加,在 Ug 为 0.35 至 0.65 m/s 时,还原时间为 4000 秒后,还原度几乎达到 100%。在 10 至 100 pct 的范围内,还原率随氢气浓度的增加而明显增加,在 65 pct 的氢气浓度条件下,4000 秒后 Fe2O3 可完全转化为 Fe。此外,氢气浓度越高,Fe2O3 的消耗和 Fe 的生成速度越快。在不同的 H2 浓度下,Fe3O4 和 FeO 的质量分数峰值范围分别为 0.29 至 0.34 和 0.21 至 0.24。
DDPM Simulation for Fluidization Behavior and Reduction of Iron Ore Fines with Hydrogen in the Fluidized Bed
In this paper, the hydrogen direct reduction of iron ore fines is numerically studied by using the Dense Discrete Phase Model (DDPM) in the fluidized bed. The fluidization behavior at different inlet gas velocities (Ug) as well as the influence of Ug and hydrogen concentration on reduction degree (RD) are comprehensively investigated. The result indicates the increase of time-averaged solids volume fraction for the same cross-sectional heights with increasing Ug when the bed height (H) exceeds 0.06 m. Furthermore, the reduction rate of mineral powder increases with higher Ug value, and the RD reaches almost 100 pct after 4000 seconds of reduction time with Ug ranging from 0.35 to 0.65 m/s. The reduction rate increases noticeably with the increase of hydrogen concentration in the range of 10 to 100 pct, and Fe2O3 can be completely converted to Fe under condition of 65 pct H2 concentration after 4000 seconds. Moreover, higher H2 concentration leads to faster rate of Fe2O3 consumption and Fe production. The mass fraction peak values of Fe3O4 and FeO are in the range of 0.29 to 0.34 and 0.21 to 0.24 under different H2 concentrations, respectively.