๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Modeling CFB biomass pyrolysis reactors

โœ Scribed by Manon Van de Velden; Jan Baeyens; Ioannis Boukis


Publisher
Elsevier Science
Year
2008
Tongue
English
Weight
410 KB
Volume
32
Category
Article
ISSN
0961-9534

No coin nor oath required. For personal study only.

โœฆ Synopsis


Fluidized bed-fast pyrolysis of biomass is considered as having a high commercial potential for the thermal treatment of biomass.

This paper mainly presents a model developed further to improvements in the understanding of the science, and capable of predicting pyrolysis yields that are in satisfactory agreement with literature data.

The kinetics and endothermicity of biomass pyrolysis are reviewed from extensive TGA and differential scanning calorimetry experiments. For most biomass species, the reaction rate constant is 40.5 s ร€1 , corresponding to a fast reaction, so the requirement of a short reaction time for a high conversion can be met. Lab-scale batch experiments and pilotscale CFB experiments show that an oil yield between 60 and 70 wt% can be achieved at an operating temperature of 510710 1C, in line with literature data. Pyrolysis fundamentals are the basis of the developed model, applied to predict the yields of the different products as functions of process operation variables. The predictions are in fair agreement with our own conversion experiments and literature data. Finally, all findings are used and are illustrated in the design strategy of a CFB for the pyrolysis of biomass.


๐Ÿ“œ SIMILAR VOLUMES


Reactor for drying, pyrolysis, and gasif
๐Ÿ“‚ Article ๐Ÿ“… 2002 ๐Ÿ› Elsevier Science โš– 173 KB

03 Gaseous fuels (derived gaseous fuels) concentration gradients. The catalyst is supported on a ceramic or metal monolith. The reactor may also have reaction zones for conducting water gas shift reaction and catalytic oxidation. ## 02lOO379 Reactor for drying, pyrolysis, and gasification of a bi

new improvements in modeling kinetic sch
โœ M. Dente; S. Pierucci; E. Ranzi; G. Bussani ๐Ÿ“‚ Article ๐Ÿ“… 1992 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 556 KB

In recent years, significant improvements have been reached both in the technology of hydrocarbons pyrolysis for olefines production and in the modeling of the kinetic schemes involved. Some of the reasons for these improvements are: -New sophisticated instrumentation for continuous analysis of effl