Abstract
In dual fluidized bed gasification technology, the gasification/pyrolysis and combustion reactions are decoupled and conducted in two separate fluidized bed reactors connected by circulating inert or catalytic bed material. Hence, a nitrogen-free high-quality syngas is produced. The configuration obviates the need of a capital-intensive air separation unit. It is a complex reactor system, and the challenge lies in selecting appropriate bed material/catalyst, understanding flow patterns and heat transfer characteristics, and designing and operating such a system. This chapter reviews the basic concept, critical components, hydrodynamics, and process characteristics of this technology presenting the current state of the art.
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Abbreviations
- AER:
-
Adsorption Enhanced Reforming
- BFB:
-
Bubbling Fluidized Bed
- CFB:
-
Circulating Fluidized Bed
- CFM:
-
Cold Flow Model
- CV:
-
Calorific Value
- db:
-
Dry basis
- DFB:
-
Dual Fluidized Bed
- DFBG:
-
Dual Fluidized Bed Gasifier
- ECN:
-
Energy Research Center of the Netherlands
- FT:
-
Fischer Tropsch
- HDS:
-
Hydrodesulfurization
- PAH:
-
Polycyclic Aromatic Hydrocarbons
- SNG:
-
Synthetic Natural gas
- VTU:
-
Vienna University of Technology (TU Wien)
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Acknowledgements
The authors would like to acknowledge joint financial support from Ministry of Human Resource and Development and Ministry of Coal under the IMPRINT initiative by Government of India (Project No: MHRD/ME/2016408B, Title: Development of pressurized dual fluidized bed gasifier for high-ash Indian coal)
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Bhaskaran, S., Gupta, S., De, S. (2018). Dual Fluidized Bed Gasification of Solid Fuels. In: De, S., Agarwal, A., Moholkar, V., Thallada, B. (eds) Coal and Biomass Gasification. Energy, Environment, and Sustainability. Springer, Singapore. https://doi.org/10.1007/978-981-10-7335-9_17
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