Gasification of refuse-derived fuel

Kuen Song Lin; Hong-Paul Wang; Ni Bin Chang; C. J.G. Jou

Gasification of refuse-derived fuel

Kuen Song Lin, Hong-Paul Wang, Ni Bin Chang, C. J.G. Jou

環境工程學系

研究成果: Conference article › 同行評審

1 引文斯高帕斯（Scopus）

摘要

Refuse-derived fuel (RDF) was mechanically separated from MSW in a 300 TPD (tons per day) waste pretreatment plant. Refuse-derived fuel represents a significant quantity of energy. Recovery of part of this energy content in a form of syngas would be environmentally attractive. Gasification of RDF was conducted in a thermal gravimetric analyzer (TGA) to obtain the data of thermal degradation kinetics. At least two main distinct weight loss stages in the TGA feature are found for RDF gasification. About >92% (dry basis) of hydrogen (H₂) and carbon monoxide (CO) were generated at 1473 K and 40.85 atm in a 0.465 m³ gasifier. In addition to the syngas generation, approximately 4.35×10⁶ kcal/hr of thermal energy may be recovered from the RDF gasification process. The cold gas efficiency (CGE) of the RDF gasification was 79-84%, which may be improved by operating the gasification at an O/C atomic ratio between 1.00 to 1.20.

原文	English
頁（從 - 到）	617-621
頁數	5
期刊	Proceedings of the International Conference on Solid Waste Technology and Management
出版狀態	Published - 1999 12月 1
事件	Proceedings of the International Conference on Solid Waste Technology and Mangement - Philadelphia, PA, USA 持續時間: 1999 12月 12 → 1999 12月 15

All Science Journal Classification (ASJC) codes

環境工程
廢物管理和處置

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@article{4960b42565e14e2bb32cdd29b1207650,

title = "Gasification of refuse-derived fuel",

abstract = "Refuse-derived fuel (RDF) was mechanically separated from MSW in a 300 TPD (tons per day) waste pretreatment plant. Refuse-derived fuel represents a significant quantity of energy. Recovery of part of this energy content in a form of syngas would be environmentally attractive. Gasification of RDF was conducted in a thermal gravimetric analyzer (TGA) to obtain the data of thermal degradation kinetics. At least two main distinct weight loss stages in the TGA feature are found for RDF gasification. About >92% (dry basis) of hydrogen (H2) and carbon monoxide (CO) were generated at 1473 K and 40.85 atm in a 0.465 m3 gasifier. In addition to the syngas generation, approximately 4.35×106 kcal/hr of thermal energy may be recovered from the RDF gasification process. The cold gas efficiency (CGE) of the RDF gasification was 79-84%, which may be improved by operating the gasification at an O/C atomic ratio between 1.00 to 1.20.",

author = "Lin, {Kuen Song} and Hong-Paul Wang and Chang, {Ni Bin} and Jou, {C. J.G.}",

year = "1999",

month = dec,

day = "1",

language = "English",

pages = "617--621",

journal = "Proceedings of the International Conference on Solid Waste Technology and Management",

issn = "1091-8043",

note = "Proceedings of the International Conference on Solid Waste Technology and Mangement ; Conference date: 12-12-1999 Through 15-12-1999",

}

TY - JOUR

T1 - Gasification of refuse-derived fuel

AU - Lin, Kuen Song

AU - Wang, Hong-Paul

AU - Chang, Ni Bin

AU - Jou, C. J.G.

PY - 1999/12/1

Y1 - 1999/12/1

N2 - Refuse-derived fuel (RDF) was mechanically separated from MSW in a 300 TPD (tons per day) waste pretreatment plant. Refuse-derived fuel represents a significant quantity of energy. Recovery of part of this energy content in a form of syngas would be environmentally attractive. Gasification of RDF was conducted in a thermal gravimetric analyzer (TGA) to obtain the data of thermal degradation kinetics. At least two main distinct weight loss stages in the TGA feature are found for RDF gasification. About >92% (dry basis) of hydrogen (H2) and carbon monoxide (CO) were generated at 1473 K and 40.85 atm in a 0.465 m3 gasifier. In addition to the syngas generation, approximately 4.35×106 kcal/hr of thermal energy may be recovered from the RDF gasification process. The cold gas efficiency (CGE) of the RDF gasification was 79-84%, which may be improved by operating the gasification at an O/C atomic ratio between 1.00 to 1.20.

AB - Refuse-derived fuel (RDF) was mechanically separated from MSW in a 300 TPD (tons per day) waste pretreatment plant. Refuse-derived fuel represents a significant quantity of energy. Recovery of part of this energy content in a form of syngas would be environmentally attractive. Gasification of RDF was conducted in a thermal gravimetric analyzer (TGA) to obtain the data of thermal degradation kinetics. At least two main distinct weight loss stages in the TGA feature are found for RDF gasification. About >92% (dry basis) of hydrogen (H2) and carbon monoxide (CO) were generated at 1473 K and 40.85 atm in a 0.465 m3 gasifier. In addition to the syngas generation, approximately 4.35×106 kcal/hr of thermal energy may be recovered from the RDF gasification process. The cold gas efficiency (CGE) of the RDF gasification was 79-84%, which may be improved by operating the gasification at an O/C atomic ratio between 1.00 to 1.20.

UR - http://www.scopus.com/inward/record.url?scp=0033292280&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=0033292280&partnerID=8YFLogxK

M3 - Conference article

AN - SCOPUS:0033292280

SN - 1091-8043

SP - 617

EP - 621

JO - Proceedings of the International Conference on Solid Waste Technology and Management

JF - Proceedings of the International Conference on Solid Waste Technology and Management

T2 - Proceedings of the International Conference on Solid Waste Technology and Mangement

Y2 - 12 December 1999 through 15 December 1999

ER -

Gasification of refuse-derived fuel

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All Science Journal Classification (ASJC) codes

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