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Journal ArticleDOI

A review of the primary measures for tar elimination in biomass gasification processes

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TLDR
In this paper, a review of the research and development in this area are reviewed and cited in the present paper, and the concepts of two-stage gasification and secondary air injection in the gasifier are of prime importance.
Abstract
Tar formation is one of the major problems to deal with during biomass gasification. Tar condenses at reduced temperature, thus blocking and fouling process equipments such as engines and turbines. Considerable efforts have been directed on tar removal from fuel gas. Tar removal technologies can broadly be divided into two approaches; hot gas cleaning after the gasifier (secondary methods), and treatments inside the gasifier (primary methods). Although secondary methods are proven to be effective, treatments inside the gasifier are gaining much attention as these may eliminate the need for downstream cleanup. In primary treatment, the gasifier is optimized to produce a fuel gas with minimum tar concentration. The different approaches of primary treatment are (a) proper selection of operating parameters, (b) use of bed additive/catalyst, and (c) gasifier modifications. The operating parameters such as temperature, gasifying agent, equivalence ratio, residence time, etc. play an important role in formation and decomposition of tar. There is a potential of using some active bed additives such as dolomite, olivine, char, etc. inside the gasifier. Ni-based catalyst are reported to be very effective not only for tar reduction, but also for decreasing the amount of nitrogenous compounds such as ammonia. Also, reactor modification can improve the quality of the product gas. The concepts of two-stage gasification and secondary air injection in the gasifier are of prime importance. Some aspects of primary methods and the research and development in this area are reviewed and cited in the present paper.

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Citations
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Journal ArticleDOI

Synthesis of transportation fuels from biomass: chemistry, catalysts, and engineering.

TL;DR: Hydrogen Production by Water−Gas Shift Reaction 4056 4.1.
Journal ArticleDOI

Modeling chemical and physical processes of wood and biomass pyrolysis

TL;DR: In this article, the state of the art in modeling chemical and physical processes of wood and biomass pyrolysis is reported, and the main achievements of numerical simulations are discussed.
Journal ArticleDOI

A review on pyrolysis of biomass constituents: Mechanisms and composition of the products obtained from the conversion of cellulose, hemicelluloses and lignin

TL;DR: In this article, the main steps of pyrolysis and the composition of the products obtained from each constituent were synthesized and the results were used to predict the reactivity and energy content of these products and evaluate their potential use as biofuels in renewable applications.
Book

Biomass Gasification and Pyrolysis: Practical Design and Theory

Prabir Basu
TL;DR: In this article, the authors provide a comprehensive coverage of the design, analysis, and operational aspects of biomass gasification, the key technology enabling the production of biofuels from all viable sources.
Journal ArticleDOI

Process and technological aspects of municipal solid waste gasification. A review

TL;DR: The analysis indicates that gasification is a technically viable option for the solid waste conversion, including residual waste from separate collection of municipal solid waste, and can have a remarkable effect on reduction of landfill disposal option.
References
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Journal ArticleDOI

Multi-stage reactor for thermal gasification of wood

TL;DR: In this article, a two-stage multi-stage reactor was developed in order to separate the flaming-pyrolysis zone from the reduction zone, where tar vapors generated in the first zone are burned or cracked to simple molecules by high temperature in the second zone.
Book ChapterDOI

The FICFB — Gasification Process

TL;DR: In this paper, a fluidized bed gasification reactor was developed to get a product gas with a high calorific value (up to 15 MJ/Nm3) and nearly free of nitrogen.
Journal ArticleDOI

CO2 as a gasifying agent for gas production from pine sawdust at low temperatures using a Ni/Al coprecipitated catalyst

TL;DR: In this paper, the influence of the Ni/Al catalyst weight/biomass flow rate (W/mb) ratio on product distribution and gas composition was analyzed for catalytic CO2 gasification of pine sawdust.
Journal ArticleDOI

A study on wood gasification for low-tar gas production

TL;DR: In this paper, the authors present results of an experimental study on two-stage wood gasification and attempts to reduce the tar content of the gas, which was in the range 19-34 mg/Nm3 for a charcoal gasifier coupled with a two-staged wood gasifier.
Journal ArticleDOI

Kinetics of Ammonia Decomposition in Hot Gas Cleaning

TL;DR: In this article, a kinetic model for ammonia decomposition was developed and experiments were carried out in a fixed-bed reactor dt 200-1000 degrees C, 21 atm.
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