The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass Gasifier

Tar formation is the main bottleneck for biomass gasification technology. A novel rotary kiln type biomass gasification process was proposed. The concept design was based on air staging and process separation. This concept was demonstrated on a pilot scale rotary kiln reactor under ambient pressure...

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Main Authors: Huiyuan Shi, Wen Si, Xi Li
Format: Article
Language:English
Published: MDPI AG 2016-01-01
Series:Energies
Subjects:
Online Access:http://www.mdpi.com/1996-1073/9/2/67
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spelling doaj-ef6295377f83482485d0b30aafcaadfa2020-11-24T23:15:34ZengMDPI AGEnergies1996-10732016-01-01926710.3390/en9020067en9020067The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass GasifierHuiyuan Shi0Wen Si1Xi Li2Department of Environmental Science and Engineering, Fudan University, Shanghai 200433, ChinaCollege of Information and Computer Science, Shanghai Business School, Shanghai 200235, ChinaDepartment of Environmental Science and Engineering, Fudan University, Shanghai 200433, ChinaTar formation is the main bottleneck for biomass gasification technology. A novel rotary kiln type biomass gasification process was proposed. The concept design was based on air staging and process separation. This concept was demonstrated on a pilot scale rotary kiln reactor under ambient pressure and autothermic conditions. The pilot scale gasifier was divided into three different reaction regions, which were oxidative degradation, partial oxidation and char gasification. A series of tests was conducted to investigate the effect of key parameters. The results indicate that under optimum operating conditions, a fuel gas with high heat value of about 5500 kJ/Nm3 and gas production rate of 2.32 Nm3/kg could be produced. Tar concentration in the fuel gas could be reduced to 108 mg/Nm3 (at the gasifier outlet) and 38 mg/Nm3 (after gas conditioning). The cold gas efficiency and carbon conversion rate reached 75% and 78%, respectively. The performance of this gasification system shows considerable potential for implementation in distributed electricity and heat supply projects.http://www.mdpi.com/1996-1073/9/2/67biomass gasificationair stagedrotary kilnpartial oxidationenergy balance
collection DOAJ
language English
format Article
sources DOAJ
author Huiyuan Shi
Wen Si
Xi Li
spellingShingle Huiyuan Shi
Wen Si
Xi Li
The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass Gasifier
Energies
biomass gasification
air staged
rotary kiln
partial oxidation
energy balance
author_facet Huiyuan Shi
Wen Si
Xi Li
author_sort Huiyuan Shi
title The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass Gasifier
title_short The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass Gasifier
title_full The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass Gasifier
title_fullStr The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass Gasifier
title_full_unstemmed The Concept, Design and Performance of a Novel Rotary Kiln Type Air-Staged Biomass Gasifier
title_sort concept, design and performance of a novel rotary kiln type air-staged biomass gasifier
publisher MDPI AG
series Energies
issn 1996-1073
publishDate 2016-01-01
description Tar formation is the main bottleneck for biomass gasification technology. A novel rotary kiln type biomass gasification process was proposed. The concept design was based on air staging and process separation. This concept was demonstrated on a pilot scale rotary kiln reactor under ambient pressure and autothermic conditions. The pilot scale gasifier was divided into three different reaction regions, which were oxidative degradation, partial oxidation and char gasification. A series of tests was conducted to investigate the effect of key parameters. The results indicate that under optimum operating conditions, a fuel gas with high heat value of about 5500 kJ/Nm3 and gas production rate of 2.32 Nm3/kg could be produced. Tar concentration in the fuel gas could be reduced to 108 mg/Nm3 (at the gasifier outlet) and 38 mg/Nm3 (after gas conditioning). The cold gas efficiency and carbon conversion rate reached 75% and 78%, respectively. The performance of this gasification system shows considerable potential for implementation in distributed electricity and heat supply projects.
topic biomass gasification
air staged
rotary kiln
partial oxidation
energy balance
url http://www.mdpi.com/1996-1073/9/2/67
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