Computational Fluid Dynamics Modeling of Palm Fruit Pyrolysis in a Fast Fluidized Bed Reactor

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The palm fruit biomass is introduced into the pyrolysis reactor bed and the transport equations for heat, mass and momentum transfer are solved using computational fluid dynamics (CFD) technique. The Eulerian-Eulerian approach is employed to model fluidizing behavior of the sand for an externally heated reactor prior to the introduction of the biomass. The particle motion in the reactor is computed using the drag laws which depend on the local volume fraction of each phase. Heat transfer from the fluidized bed to the biomass particles together with the pyrolysis reactions were simulated by Fluent CFD code through user-defined function (UDF). Spontaneous production of pyrolysis oil, char and non-condensable gases (NCG) confirm the observation widely reported in literature. The computer model can potentially be used to assess other candidate biomass sources also to assist design of optimized pyrolysis reactors.

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822-828

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May 2013

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] S. Czernik and A. Bridgwater: V Energy Fuels 2004, 18, 590–598.

Google Scholar

[2] G. V. Huber, S. Iborra, A. Corma:. Chem. ReV. 2006, 106, 4044–4098.

Google Scholar

[3] D. M. Snider, P. J. O'Rourke and M. J. Andrews: Sediment Flow in Inclined Vessels Calculated Using Multiphase Particle-in-Cell Model for Dense Particle Flows, Int. J. Multiphase Flow, (1998) 24, 1359-1352

DOI: 10.1016/s0301-9322(98)00030-5

Google Scholar

[4] C. C. Pain, S. Mansoorzadeh, J. L. M. Gomes, C. R. E. de Oliveira: A numerical investigation of bubbling gas–solid fluidized bed dynamics in 2-D geometries. Powder Technology 128 (1), (2002) 56–77.

DOI: 10.1016/s0032-5910(02)00167-5

Google Scholar

[5] H. Gerhauser, S. C. Generalis, R. A. Hague A. V. Bridgwater: CFD for the Modeling of Entrainment in Fluidized Bed Fast Pyrolysis of Biomass; Progress in Thermochemical Biomass Conversion, (Blackwell, Oxford, UK 2001), pp.1281-1295

DOI: 10.1002/9780470694954.ch106

Google Scholar

[6] A. A. Boateng, D.E. Daugaard, N.M. Goldberg, K.B. Hicks: Bench-Scale fluidized bed pyrolysis of switch grass for bio-oil production; Ind. Eng. Chem. Res. 2007, 46, 1891-1897

DOI: 10.1021/ie0614529

Google Scholar

[7] D. R. Gidaspow and J. Ding: Hydrodynamics of Circulating Fluidized Beds, Kinetic Theory Approach in Fluidization VII, Proceedings of the 7th, Engineering Foundation Conference on Fluidization, 75{82), 1992.

Google Scholar

[8] C. D. Blasi: Modeling chemical and physical processes of wood and biomass pyrolysis. Progress in Energy and Combustion Science 2008, 34, 47-90.

DOI: 10.1016/j.pecs.2006.12.001

Google Scholar

[9] S. A. Mohamad: Pyrolysis of Empty Oil Palm Fruit Bunches Using the Quartz Fluidized- Fixed Bed Reactor MSc. Thesis (2008)

Google Scholar

[10] T. B. Reed and B. A. Levie: A Simplified Model of the Stratified Downdraft Gasifer, Draft Report, Solar Energy Research Institute, Golden Colorado. (1983).

Google Scholar

[11] A. A. Boateng and P. L. Mtui: CFD Modeling of space-time evolution of fast pyrolysis products in bench-scale fluidized bed reactor. Applied Thermal Engineering 33-34 (2012) 190-198

DOI: 10.1016/j.applthermaleng.2011.09.034

Google Scholar