Optimization fluidization characteristics conditions of nickel oxide for hydrogen reduction by fluidized bed reactor

被引:0
|
作者
Jae-Rang Lee
Naim Hasolli
Seong-Min Jeon
Kang-San Lee
Kwang-Deuk Kim
Yong-Ha Kim
Kwan-Young Lee
Young-Ok Park
机构
[1] Korea Institute of Energy Research,Climate Change Research Division
[2] Pukyong National University,Department of Chemical Engineering
[3] Korea University,Department of Chemical Biological Engineering
来源
关键词
Fluidized Bed Reactor; Superficial Gas Velocity; Hydrogen Reduction; Reduction Rate; Pressure Drop;
D O I
暂无
中图分类号
学科分类号
摘要
We evaluated the optimal conditions for fluidization of nickel oxide (NiO) and its reduction into high-purity Ni during hydrogen reduction in a laboratory-scale fluidized bed reactor. A comparative study was performed through structural shape analysis using scanning electron microscopy (SEM); variance in pressure drop, minimum fluidization velocity, terminal velocity, reduction rate, and mass loss were assessed at temperatures ranging from 400 to 600 °C and at 20, 40, and 60 min in reaction time. We estimated the sample weight with most active fluidization to be 200 g based on the bed diameter of the fluidized bed reactor and height of the stocked material. The optimal conditions for NiO hydrogen reduction were found to be height of sample H to the internal fluidized bed reactor diameter D was H/D=1, reaction temperature of 550 °C, reaction time of 60 min, superficial gas velocity of 0.011 m/s, and pressure drop of 77 Pa during fluidization. We determined the best operating conditions for the NiO hydrogen reduction process based on these findings.
引用
收藏
页码:2321 / 2326
页数:5
相关论文
共 50 条
  • [31] Fluidization of fine powder assisted by vertical vibration in fluidized bed reactor
    Lee, Jae-Rang
    Hasolli, Naim
    Lee, Kang-San
    Lee, Kwan-Young
    Park, Young-Ok
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2019, 36 (09) : 1548 - 1556
  • [32] Optimization of the fluidized bed for crystallization process: seed fluidization study
    Jiang, Ke
    Zhou, Kanggen
    DESALINATION AND WATER TREATMENT, 2019, 155 : 162 - 167
  • [33] Fluidization characteristics of wide-size-distribution particles in a gas-solid fluidized bed reactor
    Li, Chaojie
    Wang, Weiwen
    Guo, Xiuling
    Duan, Jihai
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2020, 18 (12)
  • [34] KINETICS OF REDUCTION OF FERROUS OXIDE WITH HYDROGEN IN A FLUIDIZED BED AT STEADY STATE
    FEINMAN, J
    DREXLER, TD
    AICHE JOURNAL, 1961, 7 (04) : 584 - 587
  • [35] Fluidization characteristics of different sizes of quartz particles in the fluidized bed
    Zi-Jian Wang
    Jun Tang
    Chun-Xi Lu
    Petroleum Science, 2016, (03) : 584 - 591
  • [36] Effect of agitation on fluidization characteristics of fine particles in a fluidized bed
    Kim, Jimin
    Han, Gui Young
    POWDER TECHNOLOGY, 2006, 166 (03) : 113 - 122
  • [37] FLUIDIZATION CHARACTERISTICS OF A CIRCULATING FLUIDIZED-BED WITH AN INTERNAL NOZZLE
    HATTORI, M
    MATSUDA, H
    NOWAK, W
    HASATANI, M
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1992, 25 (05) : 592 - 597
  • [38] Fluidization characteristics of magnetic particles and determination of stable fluidization zone in magnetically fluidized bed
    School of Energy and Power Engineering, Jiangsu University, Zhenjiang 212013, China
    不详
    J. Southeast Univ. Engl. Ed., 2006, 4 (523-527):
  • [39] Fluidization characteristics of different sizes of quartz particles in the fluidized bed
    Zi-Jian Wang
    Jun Tang
    Chun-Xi Lu
    Petroleum Science, 2016, 13 (03) : 584 - 591
  • [40] Bubble characteristics in a pulsated fluidized bed under intermittent fluidization
    Nishimura, A
    Deguchi, S
    Matsuda, H
    Hasatani, M
    Mujumdar, AS
    KAGAKU KOGAKU RONBUNSHU, 2000, 26 (01) : 88 - 93