Modelling of combustion and sorbent reactions in three-dimensional flow environment of a circulating fluidized bed furnace


Autoria(s): Myöhänen, Kari
Data(s)

16/11/2011

16/11/2011

02/12/2011

Resumo

This thesis presents a three-dimensional, semi-empirical, steady state model for simulating the combustion, gasification, and formation of emissions in circulating fluidized bed (CFB) processes. In a large-scale CFB furnace, the local feeding of fuel, air, and other input materials, as well as the limited mixing rate of different reactants produce inhomogeneous process conditions. To simulate the real conditions, the furnace should be modelled three-dimensionally or the three-dimensional effects should be taken into account. The only available methods for simulating the large CFB furnaces three-dimensionally are semi-empirical models, which apply a relatively coarse calculation mesh and a combination of fundamental conservation equations, theoretical models and empirical correlations. The number of such models is extremely small. The main objective of this work was to achieve a model which can be applied to calculating industrial scale CFB boilers and which can simulate all the essential sub-phenomena: fluid dynamics, reactions, the attrition of particles, and heat transfer. The core of the work was to develop the model frame and the required sub-models for determining the combustion and sorbent reactions. The objective was reached, and the developed model was successfully used for studying various industrial scale CFB boilers combusting different types of fuel. The model for sorbent reactions, which includes the main reactions for calcitic limestones, was applied for studying the new possible phenomena occurring in the oxygen-fired combustion. The presented combustion and sorbent models and principles can be utilized in other model approaches as well, including other empirical and semi-empirical model approaches, and CFD based simulations. The main achievement is the overall model frame which can be utilized for the further development and testing of new sub-models and theories, and for concentrating the knowledge gathered from the experimental work carried out at bench scale, pilot scale and industrial scale apparatus, and from the computational work performed by other modelling methods.

Identificador

978-952-265- 161-7

1456-4491

http://www.doria.fi/handle/10024/72463

URN:ISBN:978-952-265-161-7

Idioma(s)

en

Publicador

Lappeenranta University of Technology

Relação

978-952-265-160-0

Acta Universitatis Lappeenrantaensis

Palavras-Chave #circulating fluidized bed #comprehensive model #steady state #large-scale modelling #3D #combustion #limestone #sulphur capture
Tipo

Väitöskirja

Doctoral Dissertation