DocumentCode
527176
Title
Notice of Retraction
Fuel gas production from catalytic steam gasification of municipal solid wastes
Author
Jianjun Liu ; Jianfen Li ; Shiyan Liao
Author_Institution
Sch. of Chem. & Environ. Eng., Wuhan Polytech. Univ., Wuhan, China
Volume
3
fYear
2010
fDate
17-18 July 2010
Firstpage
652
Lastpage
655
Abstract
Notice of Retraction
After careful and considered review of the content of this paper by a duly constituted expert committee, this paper has been found to be in violation of IEEE´s Publication Principles.
We hereby retract the content of this paper. Reasonable effort should be made to remove all past references to this paper.
The presenting author of this paper has the option to appeal this decision by contacting TPII@ieee.org.
The catalytic steam gasification of municipal solid wastes (MSW) for fuel gas production was experimentally investigated in a combined fixed bed reactor using the newly developed nano-NiO/γ-Al2O3 catalyst. A series of experiments have been performed to explore the effects of catalyst presence, catalytic temperature, steam to MSW ratio (S/M) and MSW particle size on the composition and yield of gasification gases. The experiments results indicated that the supported NiO/γ-Al2O3 catalyst had a high activity of cracking tar and hydrocarbons as well as upgrading the gas quality in catalytic steam gasification of municipal solid wastes. Catalytic temperature was crucial for the overall gasifiation process, a higher temperature contributed to more hydrogen production and gas yield. Comparing with MSW catalytic gasification, the introduction of steam improved gas quality and yield, the S/M ratio of 1.33 was found as the optimum operating condition in the catalytic steam gasification of municipal solid wastes. It was also shown that a smaller particle was more favorable for gas quality and yield.
After careful and considered review of the content of this paper by a duly constituted expert committee, this paper has been found to be in violation of IEEE´s Publication Principles.
We hereby retract the content of this paper. Reasonable effort should be made to remove all past references to this paper.
The presenting author of this paper has the option to appeal this decision by contacting TPII@ieee.org.
The catalytic steam gasification of municipal solid wastes (MSW) for fuel gas production was experimentally investigated in a combined fixed bed reactor using the newly developed nano-NiO/γ-Al2O3 catalyst. A series of experiments have been performed to explore the effects of catalyst presence, catalytic temperature, steam to MSW ratio (S/M) and MSW particle size on the composition and yield of gasification gases. The experiments results indicated that the supported NiO/γ-Al2O3 catalyst had a high activity of cracking tar and hydrocarbons as well as upgrading the gas quality in catalytic steam gasification of municipal solid wastes. Catalytic temperature was crucial for the overall gasifiation process, a higher temperature contributed to more hydrogen production and gas yield. Comparing with MSW catalytic gasification, the introduction of steam improved gas quality and yield, the S/M ratio of 1.33 was found as the optimum operating condition in the catalytic steam gasification of municipal solid wastes. It was also shown that a smaller particle was more favorable for gas quality and yield.
Keywords
catalysis; catalysts; chemical reactors; hydrogen production; particle size; steam reforming; waste handling; MSW particle size; catalytic steam gasification; catalytic temperature; combined fixed bed reactor; cracking tar; fuel gas production; gas quality; gas yield; gasification gases; hydrocarbons; hydrogen production; municipal solid wastes; nanocatalyst; operating condition; Ash; Biomass; Chemicals; Global warming; Loading; Production; Solids; Biomass gasification; catalyst; hydrogen production; municipal solid wastes;
fLanguage
English
Publisher
ieee
Conference_Titel
Environmental Science and Information Application Technology (ESIAT), 2010 International Conference on
Conference_Location
Wuhan
Print_ISBN
978-1-4244-7387-8
Type
conf
DOI
10.1109/ESIAT.2010.5568434
Filename
5568434
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