Pyrolysis of RDF and Catalytic Decomposition of the Produced Tar in a Char Bed Secondary Reactor as an Efficient Source of Syngas
Abstract
One of the technical limitations of refuse-derived fuel (RDF) pyrolysis is the high content of tar in its gas products. In order to resolve this problem, a two-stage RDF pyrolysis with a catalyst based on char from RDF pyrolysis is proposed. This paper presents the results of municipal waste pyrolysis beginning in an oven heated to 480 °C and ending with catalytic tar cracking carried out in the temperature range from 800 to 1000 °C. Thermal and catalytic pyrolysis with a char catalyst containing a minimum of 6% Fe resulted in increases in the CO and H2 contents in gas products and decreases in CO2 and CH4. At 1000 °C, the mass ratio of gaseous products to liquids was greater than 6. The residence time of the gases in the catalytic zone was about 3–5 s. The reactor was a good source of hydrogen and carbon monoxide.
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- DOI:
- Digital Object Identifier (open in new tab) 10.3390/pr10010090
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- Category:
- Articles
- Type:
- artykuły w czasopismach
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Processes
no. 10,
ISSN: 2227-9717 - Language:
- English
- Publication year:
- 2022
- Bibliographic description:
- Kusz B., Kardaś D., Heda Ł., Trawiński B.: Pyrolysis of RDF and Catalytic Decomposition of the Produced Tar in a Char Bed Secondary Reactor as an Efficient Source of Syngas// Processes -Vol. 10,iss. 10 (2022), s.90-
- DOI:
- Digital Object Identifier (open in new tab) 10.3390/pr10010090
- Verified by:
- Gdańsk University of Technology
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