Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formation
In this study, municipal solid waste (MSW) from a dumpsite was converted into refuse derived fuel (RDF) and used as feedstock for an air-blown gasification process. The gasification process was conducted in a 10 kg.hr -1 downdraft gasifier at different air flow rates of 300, 350, 400, 450 and 550...
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Prince of Songkla University
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doaj-2400a8ec0adf4922ae4223dc3c4476a22020-11-24T22:53:31ZengPrince of Songkla UniversitySongklanakarin Journal of Science and Technology (SJST)0125-33952016-04-01382221228Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formationTabitha Geoffrey Etutu0Krongkaew Laohalidanond1Somrat Kerdsuwan2The Waste Incineration Research Center, Department of Mechanical and Aerospace Engineering, Faculty of Engineering, King Mongkut’s University of Technology North Bangkok, Bang Sue, Bangkok, 10800 Thailand.The Waste Incineration Research Center, Department of Mechanical and Aerospace Engineering, Faculty of Engineering, King Mongkut’s University of Technology North Bangkok, Bang Sue, Bangkok, 10800 Thailand.The Waste Incineration Research Center, Department of Mechanical and Aerospace Engineering, Faculty of Engineering, King Mongkut’s University of Technology North Bangkok, Bang Sue, Bangkok, 10800 Thailand.In this study, municipal solid waste (MSW) from a dumpsite was converted into refuse derived fuel (RDF) and used as feedstock for an air-blown gasification process. The gasification process was conducted in a 10 kg.hr -1 downdraft gasifier at different air flow rates of 300, 350, 400, 450 and 550 NL.min1 at atmospheric pressure in order to investigate the quantity and quality of tar formed. It was shown that the increase in the air flow rate from 300 NL.min1 to 550 NL.min1 led to an increase in the oxidation temperature from 719°C to 870°C and an increase in the reduction temperature from 585°C to 750°C, respectively. Tar was reduced from 15 g.Nm3 to 4.7 g.Nm3 respectively. Heavy tar compounds (>C17) e.g. pyrene and phenathrene, decreased with the increase in the light tar compounds (<C10) e.g. naphthalene, indene and toluene; indicating the presence tar reduction through a tar cracking process.http://rdo.psu.ac.th/sjstweb/journal/38-2/38-2-15.pdftar formationtar reductionair blown gasificationdowndraft gasifier |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Tabitha Geoffrey Etutu Krongkaew Laohalidanond Somrat Kerdsuwan |
spellingShingle |
Tabitha Geoffrey Etutu Krongkaew Laohalidanond Somrat Kerdsuwan Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formation Songklanakarin Journal of Science and Technology (SJST) tar formation tar reduction air blown gasification downdraft gasifier |
author_facet |
Tabitha Geoffrey Etutu Krongkaew Laohalidanond Somrat Kerdsuwan |
author_sort |
Tabitha Geoffrey Etutu |
title |
Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formation |
title_short |
Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formation |
title_full |
Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formation |
title_fullStr |
Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formation |
title_full_unstemmed |
Gasification of municipal solid waste in a downdraft gasifier: Analysis of tar formation |
title_sort |
gasification of municipal solid waste in a downdraft gasifier: analysis of tar formation |
publisher |
Prince of Songkla University |
series |
Songklanakarin Journal of Science and Technology (SJST) |
issn |
0125-3395 |
publishDate |
2016-04-01 |
description |
In this study, municipal solid waste (MSW) from a dumpsite was converted into refuse derived fuel (RDF) and used as
feedstock for an air-blown gasification process. The gasification process was conducted in a 10 kg.hr
-1 downdraft gasifier at
different air flow rates of 300, 350, 400, 450 and 550 NL.min1
at atmospheric pressure in order to investigate the quantity and
quality of tar formed. It was shown that the increase in the air flow rate from 300 NL.min1
to 550 NL.min1
led to an increase in
the oxidation temperature from 719°C to 870°C and an increase in the reduction temperature from 585°C to 750°C, respectively.
Tar was reduced from 15 g.Nm3
to 4.7 g.Nm3
respectively. Heavy tar compounds (>C17) e.g. pyrene and phenathrene,
decreased with the increase in the light tar compounds (<C10) e.g. naphthalene, indene and toluene; indicating the presence
tar reduction through a tar cracking process. |
topic |
tar formation tar reduction air blown gasification downdraft gasifier |
url |
http://rdo.psu.ac.th/sjstweb/journal/38-2/38-2-15.pdf |
work_keys_str_mv |
AT tabithageoffreyetutu gasificationofmunicipalsolidwasteinadowndraftgasifieranalysisoftarformation AT krongkaewlaohalidanond gasificationofmunicipalsolidwasteinadowndraftgasifieranalysisoftarformation AT somratkerdsuwan gasificationofmunicipalsolidwasteinadowndraftgasifieranalysisoftarformation |
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