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