Issue
Korean Journal of Chemical Engineering,
Vol.35, No.11, 2321-2326, 2018
Optimization fluidization characteristics conditions of nickel oxide for hydrogen reduction by fluidized bed reactor
We evaluated the optimal conditions for fluidization of nickel oxide (NiO) and its reduction into highpurity 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.
[References]
  1. Mentus S, Tomic-Tucakovic B, Majstorovic D, Dimitrijevic R, Mater. Chem. Phys., 112(1), 254, 2008
  2. Szekely J, Lin CI, Sohn HY, Chem. Eng. Sci., 28, 1975, 1973
  3. Da Costa AR, Wagner D, Patisson F, J. Clean Prod., 46, 27, 2013
  4. Zhang B, Wang Z, Gong XZ, Guo ZC, Powder Technol., 225, 1, 2012
  5. Plascencia G, Utigard T, Chem. Eng. Sci., 64, 2879, 2009
  6. Carlson A, Energy Policy, 31(10), 951, 2003
  7. Barreto L, Makihira A, Riahi K, Int. J. Hydrog. Energy, 28(3), 267, 2003
  8. Szekely J, Evans JW, Metall. Mater. Trans., 2, 1699, 1971
  9. Rhodes MJ, Geldart D, Powder Technol., 53, 155, 1987
  10. Pacek AW, Nienow AW, Powder Technol., 60, 145, 1990
  11. Iida Y, Shimada K, Bull. Chem. Soc. Jpn., 33, 8, 1960
  12. Utigard TA, Wu M, Plascencia G, Marin T, Chem. Eng. Sci., 60(7), 2061, 2005
  13. Li J, Luo GH, Wei F, Powder Technol., 229, 152, 2012
  14. Geldart D, Powder Technol., 7, 285, 1973
  15. Qian GH, Bagyi I, Burdick IW, Pfeffer R, Shaw H, Stevens JG, AIChE J., 47(5), 1022, 2001
  16. Geldart D, Gas Fluidization Technol., John Wiley & Sons (1986).
  17. Szekely J, Lin CI, Sohn HY, Chem. Eng. Sci., 28, 1975, 1973
  18. Kunii D, Levenspiel O, Fluidization Engineering Second Edition, Butterworth-Heinemann (1991).
  19. Grace JR, Knowlton TM, Avidan AA, Eds. Circulating fluidized beds, Springer Science and Business Media (2012).
  20. Fletcher JV, Deo MD, Hanson FV, Powder Technol., 76, 141, 1993
  21. Wu Y, He Y, Wu T, Chen T, Weng W, Wan H, Mater. Lett., 61, 3174, 2007
  22. Jankovic B, Adnadevic B, Mentus S, Chem. Eng. Sci., 63(3), 567, 2008
  23. Li J, Liu X, Zhou L, Zhu Q, Li H, Particuology, 19, 27, 2015