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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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Journal ArticleDOI

Air-Blown Entrained Flow Gasification of Biomass: Influence of Operating Conditions on Tar Generation

TL;DR: In this paper, the impact of air-blown gasification conditions and fuel properties of biocoal from hydrothermal carbonization (HTC) on tar formation were investigated using solid phase adsorption at an electrically heated entrained-flow gasifier with temperatures of 900-1300 °C and different air/fuel equivalence ratios.
Journal Article

Charcoal Yield from Urban-Tree Residues Generated in University of Ibadan, Nigeria using Earth Mound Method

TL;DR: In this article, a review on methods applied for pre-treatment of biomass for cracking down the complex polymer structure - lignocellulose into porous materials, advantages of using agriculture sludge as biomass fuel, ways to obtain a sludge feedstock composition which would not lead to tar formation during gasification process, modification of gasifier design and operating parameters, In-situ catalytic conversion methods to crack down large hydrocarbon molecules if ever they are formed, cleaning techniques to remove tar and other impurities, up-gradation of product gas to methane for higher cal
Journal ArticleDOI

In-depot upgrading the quality of fuel chips for a commercial gasification plant

TL;DR: In this article, the sensitivity of steam production rate in a commercial updraft gasifier to several critical feedstock quality attributes like moisture, ash, and particles size was quantified.
Journal ArticleDOI

Characterization of Coal Bottom Ash &its Potential to be used as Catalyst in Biomass Gasification

TL;DR: In this paper, the physicochemical properties of coal bottom ash have been studied for its application as a catalyst in biomass steam gasification and the results showed that elements like Si, Fe, Al, Ca and Mg were present in coal bottom Ash which have been previously used as a catalysts in biomass gasification.
Journal ArticleDOI

Barriers to Success: A Technical Review on the Limits and Possible Future Roles of Small Scale Gasifiers

Giulio Allesina, +1 more
- 15 Oct 2021 - 
TL;DR: In this article, the authors investigate the existing technological barriers that limit the spreading of biomass gasification from a socio-technical point of view, highlighting features, such as residual biomass use, distributed generation and carbon sequestration, that perfectly incorporate gasification into circular economies and sustainable development goals.
References
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Journal ArticleDOI

Review of literature on catalysts for biomass gasification

TL;DR: In this article, an extensive literature review of the three main groups of catalysts, which have been evaluated for the elimination of these hydrocarbons, are dolomite, alkali metals and nickel.
Journal ArticleDOI

The technical and economic feasibility of biomass gasification for power generation

TL;DR: In this paper, the costs and technologies involved in an integrated system for the production of electricity from biomass in general and wood in particular are reviewed, and the main conclusions are that wood handling, storage, drying, comminution and screening are well established and present no uncertainties in operation and performance.
Book

World energy assessment : energy and the challenge of sustainability

TL;DR: In this paper, the authors discuss the linkage between energy and economic, social, environmental, and security issues, and analyzes the contradictions between current patterns of use and objectives in these areas.
Journal ArticleDOI

Steam-gasification of biomass in a fluidised-bed of olivine particles.

TL;DR: In this paper, the catalytic behavior of olivine, a common, naturally occurring mineral containing magnesium, iron oxides and silica, was investigated in a laboratory scale, biomass gasification unit.
Journal ArticleDOI

Biomass gasification with air in an atmospheric bubbling fluidized bed. Effect of six operational variables on the quality of the produced raw gas

TL;DR: In this paper, the equivalence ratio (from 0.20 to 0.45), temperatures of the gasifier bed (750−850 °C) and of its freeboard (500−600 °C), H/C ratio in the feed, use of secondary air (10% of the overall) in the freeboard, and addition (2−5 wt %) of a calcined dolomite mixed with the biomass used as the feedstock.
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