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Numerical Simulation of Vortex Pyrolysis Reactors for Condensable Tar Production from Biomass
Author(s) -
Richard S. Miller,
Josette Bellan
Publication year - 1998
Publication title -
energy and fuels
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.861
H-Index - 186
eISSN - 1520-5029
pISSN - 0887-0624
DOI - 10.1021/ef970088a
Subject(s) - pyrolysis , mechanics , tar (computing) , turbulence , particle (ecology) , vortex , materials science , biomass (ecology) , breakup , reynolds stress , reynolds number , particle size , chemical engineering , physics , engineering , geology , oceanography , computer science , programming language
A numerical study is performed in order to evaluate the performance and optimal operating conditions of vofiex pyrolysis reactors used for condensable tar production from biomass. A detailed mathematical model of porous biomass particle pyrolysis is coupled with a compressible Reynolds stress transport model for the twbulent reactor swirling flow. An initial evaluation of particle dirnensionality effects is made through comparisons of single- (lD) and mukbdhnensional particle simulations and reveals that the lD particle model results in conwvative estimates for total pyrolysis conversion times and tar collection. The observed deviations are due predominantly to geometry effects while directional effects from thermal conductivity and permeability variations am relatively small. Rapid ablative particle heating rates are attributed to a mechanical fragmentation of the biomass particles that is modeled using a critical porosity for matrix breakup. Optimal thermal conditions for tar production are obsemxl for reactor wall temperatures of approximately 900K. Effects of biomass identity, particle size distriiutioL and reactor geome~ and scale are discussed

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