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Transforming Municipal Solid Waste (MSW) Into Fuel via the Gasification/Pyrolysis Process

[+] Author Affiliations
Eilhann Kwon, Kelly J. Westby, Marco J. Castaldi

Columbia University, New York, NY

Paper No. NAWTEC18-3559, pp. 53-60; 8 pages
doi:10.1115/NAWTEC18-3559
From:
  • 18th Annual North American Waste-to-Energy Conference
  • 18th Annual North American Waste-to-Energy Conference
  • Orlando, Florida, USA, May 11–13, 2010
  • Conference Sponsors: Solid Waste Processing Division and Environmental Engineering Division
  • ISBN: 978-0-7918-4393-2 | eISBN: 978-0-7918-3868-6
  • Copyright © 2010 by ASME

abstract

Municipal solid waste (MSW) gasification/pyrolysis enhancement using CO2 as gasification medium has been studied to understand the performance under various reaction conditions. MSW gasification/pyrolysis has been characterized thermo-gravimetrically under various atmospheres covering the gasification/pyrolysis process, which has been used as a basis for scale-up experimental work using a flow-through reactor (FTR) and drop tube reactor (DTR) (0.5 g/min of sample, 4–5 sec residence time, 500°C-1000°C). For example, FTR has been used to carry out the fast pyrolysis process having a nominal heating rate of 800°C/min. Oils produced from the FTR have been condensed and analyzed with GC/MS. Among identified chemical species in the pyrolysis sample, the 10 most abundant compounds (benzene, toluene, styrene, limonene, 2,3-dimethyl-1-heptene, benzoic acid, ethylbenzene, indole, xylene, and d-allose) in the pyrolysis oil sample were determined and quantified. These 10 abundant chemical species are substantially reduced in the presence of CO2 . This leads to a substantial increase of C1–5 hydrocarbons in gaseous (non-condensable) products and a reduction of pyrolysis oil (∼20%) as well. In addition, MSW samples have been tested in the DTR at a temperature range from 500°C and 1000°C under various atmospheres with CO2 concentrations of 0% and 30%. The release of all chemical species from the DTR was determined using μ-GC. For example, CO (∼30%), H2 (∼25%), and CH4 (∼10%) under the presence of CO2 were generated and introducing CO2 into the gasification process substantially enhanced syngas production. Finally, steam gasification using different ratios of biomass to polyethylene has been explored to better understand the enhanced steam gasification of MSW that is mostly composed of biomass and polymer. Overall thermal degradation trend is the similar, but steam gasification of MSW needs a relatively long residence time and high temperature as compared to biomass.

Copyright © 2010 by ASME

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