Steam Gasification of Municipal Solid Waste in Drop Tube Fixed Bed Reactor

• Published in: IOP conference series. Earth and environmental science 2019-05, Vol.265 (1), p.12017
• Main Authors: Sirirermrux, Nuth, Kerdsuwan, Somrat
• Format: Article
• Language: English
• Subjects: Carbon dioxide; Carbon monoxide; Clean energy; Energy; Energy conversion; Energy conversion efficiency; Energy output; Energy recovery; Fixed bed reactors; Fixed beds; Flammability; Flow rates; Flow velocity; Gasification; Hydrogen; Hydrogen production; Leather; Municipal solid waste; Municipal waste management; Polyethylene; Polyethylenes; Polypropylene; Producer gas; Reactors; Shift reaction; Solid waste management; Steam flow; Technology; Waste to energy; Water gas
• ISSN: 1755-1307; 1755-1315; 1755-1315
• DOI: 10.1088/1755-1315/265/1/012017

Waste-to-Energy (WTE) technology becomes crucial option for Municipal Solid Waste (MSW) disposal and recovery clean energy. Thermal conversion technology by steam gasification plays important key role for sustainable solution of WTE and enrich the production of Hydrogen. In this work, gasification experiment was conducted in small dropped tube fixed bed reactor by feeding surrogate MSW which including of food & kitchen waste, plastic (polyethylene & polypropylene), paper, rubber & leather, textile and biomass. The experimental conditions were varied at temperature 700, 800 and 900°C. Steam was supplied as gasifying agent with flow rate of 0.1, 0.2 and 0.3 ml/min. The main purpose was to produce hydrogen by water gas-shift reaction, nevertheless, other related producer gas e.g. carbon monoxide, methane, carbon dioxide and light hydrocarbon gas were also examined. The result showed reaction temperature 800°C with steam flow rate 0.2 ml/min offer the optimized hydrogen yield as 34.84 gh2/kgmsw whereas it trended to decrease when reaction temperature increase. In addition, the overall performance of experimental condition was evaluated by energy output and energy conversion efficiency which were calculated from volumetric of combustible gas. The minimum energy output and energy conversion efficiency were 7,638 kJ/kgsample and 31.11%, respectively, obtained at reaction temperature 700°C with steam flow rate 0.2 ml/min while the maximum value was offered by reaction temperature 900°C with same steam flow rate as 17,756 kJ/kgsample and 72.32%, respectively.