Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of Biomass

Investigation into clean energies has been focused on finding an alternative to fossil fuels in order to reduce global warming while at the same time satisfying the world’s energy needs. Biomass gasification is seen as a promising thermochemical conversion technology as it allows useful gaseous prod...

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Main Authors: María Pilar González-Vázquez, Roberto García, Covadonga Pevida, Fernando Rubiera
Format: Article
Language:English
Published: MDPI AG 2017-03-01
Series:Energies
Subjects:
Online Access:http://www.mdpi.com/1996-1073/10/3/306
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spelling doaj-f9b4808732e941b3a7122ed815e703162020-11-24T21:18:37ZengMDPI AGEnergies1996-10732017-03-0110330610.3390/en10030306en10030306Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of BiomassMaría Pilar González-Vázquez0Roberto García1Covadonga Pevida2Fernando Rubiera3Instituto Nacional del Carbón, INCAR-CSIC, Apartado 73, 33080 Oviedo, SpainInstituto Nacional del Carbón, INCAR-CSIC, Apartado 73, 33080 Oviedo, SpainInstituto Nacional del Carbón, INCAR-CSIC, Apartado 73, 33080 Oviedo, SpainInstituto Nacional del Carbón, INCAR-CSIC, Apartado 73, 33080 Oviedo, SpainInvestigation into clean energies has been focused on finding an alternative to fossil fuels in order to reduce global warming while at the same time satisfying the world’s energy needs. Biomass gasification is seen as a promising thermochemical conversion technology as it allows useful gaseous products to be obtained from low-energy-density solid fuels. Air–steam mixtures are the most commonly used gasification agents. The gasification performances of several biomass samples and their mixtures were compared. One softwood (pine) and one hardwood (chestnut), their torrefied counterparts, and other Spanish-based biomass wastes such as almond shell, olive stone, grape and olive pomaces or cocoa shell were tested, and their behaviors at several different stoichiometric ratios (SR) and steam/air ratios (S/A) were compared. The optimum SR was found to be in the 0.2–0.3 range for S/A = 75/25. At these conditions a syngas stream with 35% of H2 + CO and a gas yield of 2 L gas/g fuel were obtained, which represents a cold-gas efficiency of almost 50%. The torrefaction process does not significantly affect the quality of the product syngas. Some of the obtained chars were analyzed to assess their use as precursors for catalysts, combustion fuel or for agricultural purposes such as soil amendment.http://www.mdpi.com/1996-1073/10/3/306biomass gasificationbubbling fluidized bedbiomass mixturestorrefactionsyngasair–steam oxidationchar reuse
collection DOAJ
language English
format Article
sources DOAJ
author María Pilar González-Vázquez
Roberto García
Covadonga Pevida
Fernando Rubiera
spellingShingle María Pilar González-Vázquez
Roberto García
Covadonga Pevida
Fernando Rubiera
Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of Biomass
Energies
biomass gasification
bubbling fluidized bed
biomass mixtures
torrefaction
syngas
air–steam oxidation
char reuse
author_facet María Pilar González-Vázquez
Roberto García
Covadonga Pevida
Fernando Rubiera
author_sort María Pilar González-Vázquez
title Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of Biomass
title_short Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of Biomass
title_full Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of Biomass
title_fullStr Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of Biomass
title_full_unstemmed Optimization of a Bubbling Fluidized Bed Plant for Low-Temperature Gasification of Biomass
title_sort optimization of a bubbling fluidized bed plant for low-temperature gasification of biomass
publisher MDPI AG
series Energies
issn 1996-1073
publishDate 2017-03-01
description Investigation into clean energies has been focused on finding an alternative to fossil fuels in order to reduce global warming while at the same time satisfying the world’s energy needs. Biomass gasification is seen as a promising thermochemical conversion technology as it allows useful gaseous products to be obtained from low-energy-density solid fuels. Air–steam mixtures are the most commonly used gasification agents. The gasification performances of several biomass samples and their mixtures were compared. One softwood (pine) and one hardwood (chestnut), their torrefied counterparts, and other Spanish-based biomass wastes such as almond shell, olive stone, grape and olive pomaces or cocoa shell were tested, and their behaviors at several different stoichiometric ratios (SR) and steam/air ratios (S/A) were compared. The optimum SR was found to be in the 0.2–0.3 range for S/A = 75/25. At these conditions a syngas stream with 35% of H2 + CO and a gas yield of 2 L gas/g fuel were obtained, which represents a cold-gas efficiency of almost 50%. The torrefaction process does not significantly affect the quality of the product syngas. Some of the obtained chars were analyzed to assess their use as precursors for catalysts, combustion fuel or for agricultural purposes such as soil amendment.
topic biomass gasification
bubbling fluidized bed
biomass mixtures
torrefaction
syngas
air–steam oxidation
char reuse
url http://www.mdpi.com/1996-1073/10/3/306
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