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Conference paper

Fixed-bed staged gasification of biomass: Rate-controlled equilibrium modelling

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1Melentiev Energy Systems Institute, Russian Academy of Sciences, Russia, 664033 Irkutsk, Lermontova st., 130

Published
6 July 2016
Pages
311-318
Received
6 July 2016
DOI
10.65582/set.2015.118
Access
Open access, © 2015 Copyright WSSET
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Abstract

Biomass gasification is a technology suitable for small-scale power plants. This is a well-known and environmentally friendly way to convert biomass (such as forest and agricultural waste) into combustible fuel gas. However there are several disadvantages to overcome. Tarry gases call for a costly gas cleaning system, and the process is often unstable. These drawbacks are typical for widely used single-stage gasification processes. Staged gasification as distinct from the single-stage one allows allothermal and autothermal conversion processes to be separated within the same plant. Separation of the devolatilization and char gasification stages makes tarry volatiles to burn and produce the gasification agent. Such process organization provides both low-tar gas production and better process heat utilization. The plant being studied consists of two fixed-bed reactors and a gas combustion chamber. It has a number of feedbacks that cause a change in parameters of all reactors at a variation in any of them. A mathematical model is developed to predict staged process behaviour and to find stable operation modes. The model consists of blocks describing equilibrium gas combustion constrained by diffusion and kinetics. The results outline the control limits within which a stable and efficient gasification can be performed.

Keywords. gasification; biomass; staged process; mathematical modelling; equilibrium models; kinetic constraints

© 2015 Copyright WSSET

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