4.7 Article

Investigating biomass composition and size effects on fast pyrolysis using global sensitivity analysis and CFD simulations

Journal

CHEMICAL ENGINEERING JOURNAL
Volume 421, Issue -, Pages -

Publisher

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2020.127789

Keywords

Biomass; Pyrolysis; Fluidized bed; Kinetics; Surrogate model; Sensitivity study

Funding

  1. U.S. Department of Energy (DOE) Bioenergy Technologies Office (BETO)
  2. U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy, Bioenergy Technology Office [DE-AC36-08GO28308]
  3. Alliance for Sustainable Energy, LLC

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Building an accurate universal model for biomass pyrolysis is challenging due to its sensitivity to critical material attributes such as chemical species and physical sizes. This study implemented a biomass pyrolysis kinetics in an open-source CFD software, validated against experimental data, and showed sensitivity of pyrolysis yields to feedstock compositions through a reaction scheme with heterogeneous reactions and species. The study's results can guide the development of accurate models for fast pyrolysis reactors under various operating conditions.
It is notoriously difficult to build an accurate universal model for biomass pyrolysis due to its sensitivity to a wide number of critical material attributes such as chemical species and physical sizes. In this work, a biomass pyrolysis kinetics with 32 heterogeneous reactions and 59 species was implemented in an open-source multiphase computational fluid dynamics (CFD) software MFiX and validated against two different experimental pyrolysis data sets that provided detailed data describing chemical component yields. The reaction scheme was then used to build a surrogate model and assess the sensitivity of pyrolysis yields to feedstock compositions. The sensitivity analysis determined that the yield of bio-char showed a strong positive sensitivity to the carbon-rich lignin and tannin pseudo-species in the reaction scheme while the bio-oil and bio-gas were correlated to oxygen-rich lignin pseudo-species. The reaction scheme was then integrated into a coarse-grained discrete element model to simulate fast pyrolysis in a bubbling fluidized bed over a range of feedstock particle sizes. The reactor simulations showed further sensitivity to particle size and hydrodynamics. Notably, particles under 0.5 mm have small heat transfer limitations but left the reactor before completely converting and thus reduced the bio-oil yield. Results from this study can be used to guide future development of highly accurate models for fast pyrolysis reactors with a variety of feedstock properties and operating conditions.

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