Published in

American Chemical Society, Energy and Fuels, 2(22), p. 1380-1390, 2008

DOI: 10.1021/ef700689r

Links

Tools

Export citation

Search in Google Scholar

Mathematical modeling and experimental study of biomass combustion in a thermal 108 MW grate-fired boiler

This paper is available in a repository.
This paper is available in a repository.

Full text: Download

Green circle
Preprint: archiving allowed
  • Must obtain written permission from Editor
  • Must not violate ACS ethical Guidelines
Orange circle
Postprint: archiving restricted
  • Must obtain written permission from Editor
  • Must not violate ACS ethical Guidelines
Red circle
Published version: archiving forbidden
Data provided by SHERPA/RoMEO

Abstract

Udgivelsesdato: MAR-APR ; Grate boilers are widely used to fire biomass for heat and power production. However grate-firing systems are often reported to have relatively high un-burnout, low efficiency and high emissions, and need to be optimized and modernized. This paper presents the efforts towards a reliable baseline computational fluid dynamics (CFD) model for an industrial biomass-fired grate boiler, which can be used for diagnosis and optimization of the grate boiler as well as design of new grate boilers. First, based on the design conditions, a thorough sensitivity analysis is done to evaluate the relative importance of different factors in CFD analysis of the grate boiler. In a late stage, a two-day measuring campaign is carried out to measure the gas temperatures and gas concentrations in the boiler using a fiber optic probe connected to a Fourier transform infrared (FTIR) spectrometer. A baseline model is then defined on the basis of the sensitivity analysis and the measurements. The baseline results show an overall acceptable agreement with the measured data and the site observations, indicating the baseline model is applicable in optimization of the boiler and design of new grate boilers. However, at a few measuring locations larger discrepancies between the baseline results and the measurements are still observed. It is mainly because the boundary conditions used in the baseline model could be different from those in the real boiler. For instance, the un-continuous biomass feeding and grate movement, the combustion instabilities inside the fuel bed, and the irregular deposit formed on the furnace walls and air nozzles all make it difficult to derive the reliable boundary conditions that the CFD modeling requires. The baseline results and the measured results show the mixing and combustion behavior in the ideal furnace and in the real furnace, respectively. The local discrepancies may quantify the effect of the differences in the boundary conditions used in the baseline model and in the real boiler.