2006 AIChE Annual Meeting
(467a) Conceptual Design and Modeling of Entrained Bed Gasifier
Authors
Within the different types of gasifiers, entrained bed reactors achieve the highest gasification rates. These reactors operate with feed and blast (air/steam) in co-current flow with extremely short residence time and high temperatures and pressure. This type of gasifier generates product gas at high temperature and lowest heating value with the highest oxygen consumption.
In this work a model of a entrained bed gasifier unit has been developed for enhanced synthesis gas production. The gasification model is divided into four different stages: drying, devolatilization/pyrolysis, gasification and combustion. The conversion reactions take place sequentially. Numerical simulations are necessary to help in finding out feasible operating conditions to achieve better process performance. The introduction of solids in a process changes the heat and mass balances, even if the solid essentially passes through the process as an inert component. Aspen Plus is chosen as a simulation tool because of its capability on the solids handling. Aspen Plus includes particular physical property model and accurately represents the solid particle. In addition, FORTRAN and MATLAB calculation routines are introduced in the solution procedure. The proposed gasification model improves the understanding of the process and can be used as a predictive tool at the optimization stage.
Financial support received from the European Community projects (MRTN-CT-2004-512233; RFC-CR-04006; INCO-CT-2005-013359) and the Generalitat de Catalunya with the European Social Fund (FI grant) is fully appreciated.